CN205953925U - Multistage atomization feed nozzle - Google Patents
Multistage atomization feed nozzle Download PDFInfo
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- CN205953925U CN205953925U CN201620645198.3U CN201620645198U CN205953925U CN 205953925 U CN205953925 U CN 205953925U CN 201620645198 U CN201620645198 U CN 201620645198U CN 205953925 U CN205953925 U CN 205953925U
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Abstract
The utility model provides a multistage atomization feed nozzle, it includes shower nozzle, outer tube, inner tube, material oil inlet, steam inlet, primary steam orifice plate and a secondary steam inlet, flash steam orifice plate, the primary steam carries out the atomizing first time to raw oil in the one mixing room, get into the inner tube and carry out atomizing second time to raw oil, flash steam in the secondary mixing chamber to raw oil further strike, the breakage, atomizing for the third time promptly, get into the shower nozzle after, carry out the fourth stage and atomize, the jet exit of shower nozzle has multiple arrangement, and the broad curtain screen of formation distributes when making moisture carry -over raw materials oil spraying go out, is favorable to abundant contact, the reaction of raw oil and catalyst, the effectual breakage that reduces the catalyst simultaneously.
Description
Technical field
The utility model belongs to petroleum refining field catalytic cracking unit, relates generally to a kind of catalytic cracking of multistage atomizing
Feed nozzle.
Background technology
Raw material oil feeding atomizing nozzle is a visual plant of petroleum refining field catalytic cracking unit, and its effect is：
First feedstock oil crushed, be atomized as substantial amounts of fine drop, then raw material oil droplet is injected to catalytic cracking riser reactor
In, mix with the catalyst in riser reactor, react.Raw material oil feeding atomizing nozzle currently used for catalytic cracking unit
Form have a lot, for example, have cast, trunnion type, Y type, spiral blade profile, cone target type and all kinds of target type nozzle, domestic nozzle
There is single-tube nozzle, that is, adopt single tube chamber to feed air inlet mixed aerosol, using effect is less desirable.
Nozzle make reaction raw materials become droplet it is therefore an objective to can Quick-gasifying reacting, atomization is not final purpose,
Improve reaction effect and be only target.For the reaction result having reached, that is, need to make the liquid atomization, need to make atomization logistics again
Distribute in reactor, be critically important especially with catalyst uniform contact.
Further, since the liquid mist such as feedstock oil to be made turns to fine particle, need higher pressure drop and gas flow rate.Existing
The gas-liquid atomization logistics of technology high speed is injected directly into reactor, catalyst is washed away broken more serious.
But in actual use, said nozzle more or less has problems with：One is the atomization of feedstock oil
Effect needs to be improved further；Two is that the feedstock oil being injected in riser reactor by nozzle is not wide with catalyst contact surface,
Reaction effect is not good；Three be the atomization having nozzle to spray raw material oil droplet jet velocity too high, make catalyst breakage serious.
The utility model proposes a kind of multistage atomizing feed nozzle, make feedstock oil obtain level Four atomization, effectively eliminate big
Diameter droplets, thus reach the atomizing particle size required by catalytic cracking process.Research to shower nozzle finds, shower nozzle sprays into and carries simultaneously
The feedstock oil of riser reactors is contacted with catalyst, reacts insufficient, is because the arrangement form of conventional jet expansion is unfavorable for
The expansion of feedstock oil, the utility model proposes four kinds of nozzle structure forms, the jet expansion center line of shower nozzle both sides and nozzle
Axis angle is 0-30 °, and nozzle surface is deflected from middle part to both sides, is 0-30 ° with radial direction angle, this setting makes feedstock oil
Drip to be sprayed into from nozzle and expand to both sides after riser reactor, form broad screen, bigger with the contact surface of catalyst.Separately
Outward, jet expansion is provided with expansion segment, through circulation area expansion segment when raw material oil droplet sprays, because atomization gas density is little,
Increase with circulation area is slowed down rapidly, reduces the situation of catalyst breakage.
Utility model content
The purpose of this utility model is to provide a kind of multistage atomizing feed nozzle, and speed is varied multiple times through between gas and liquid
Degree difference, so as to enable the multistage atomizing to feedstock oil, effectively eliminates major diameter drop, is formed more when nozzle sprays simultaneously
Broad screen is so that feedstock oil is more fully contacted with catalyst, reacts；Under conditions of not affecting atomizing effect, realize
Gas-liquid is atomized the low speed contact of logistics and catalyst in reactor, reduces the erosion to catalyst and crushes.
For solving the above problems, the technical solution of the utility model is：
A kind of multistage atomizing feed nozzle, described nozzle includes shower nozzle, outer tube, inner tube, raw material oil-in, primary steam enter
Mouth, primary steam orifice plate and indirect steam entrance, indirect steam orifice plate；Described primary steam orifice plate is arranged on feedstock oil and enters
Mouthful and inner tube between, between primary steam orifice plate, raw material oil-in and inner tube formed toroidal cavity constitute primary steam room
And primary steam entrance is set, the downstream side truncated cone-shaped region of primary steam orifice plate constitutes mixed once spray chamber；Described
Indirect steam orifice plate is arranged between the expansion segment of inner tube and outer tube, forms ring between indirect steam orifice plate, outer tube and inner tube
Shape cavity constitutes indirect steam room, and arranges indirect steam entrance in indirect steam orifice plate logistics upstream, in indirect steam orifice plate
Concave regions and between shower nozzle and inner tube outlet constitute secondary mixed aerosol room；Described inner tube has shrinkage expansion range of atomization,
There are expansion segment, aditus laryngis section, contraction section；The described multiple primary steam spray orifice of primary steam orifice plate circle distribution, indirect steam
Orifice plate circle distribution multiple indirect steam spray orifice, the multiple jet expansion of shower nozzle circle distribution.
The internal tube shrinks of described multistage atomizing nozzle expand the mistake that range of atomization is gradually tapered up by multiple flow cross, expands
Cheng Zucheng, each contraction, expansion angle and each throat diameter design as needed；Shrink every time and form the acceleration of primary atomization gas simultaneously
Increase the speed difference of gas and liquid, improve liquid atomizing effect；Every time circulation area expansion formed atomization gas and gas with
The speed difference of liquid reduces, and creates conditions for again speeding up.
The primary steam orifice plate of above-mentioned multistage atomizing feed nozzle is around the port of export circle distribution M φ of raw material oil-in
The primary steam spray orifice of B, indirect steam orifice plate around the indirect steam spray orifice of the N number of φ D of inner tube expansion segment port of export circle distribution,
M, N, B, D determine, indirect steam spray orifice is corresponded with jet expansion, and that is, number, orientation are all consistent by the treating capacity of feedstock oil.
Indirect steam spray orifice can be located on inner tube expansion segment.
The shower nozzle circumference of described multistage atomizing feed nozzle arranges multiple jet expansions, and the structure setting of jet expansion is
Wikipedia type, is made up of contraction section, aditus laryngis section, expansion segment, and this structure can make feedstock oil obtain fourth stage atomization, expanding simultaneously
Open section and form deceleration area, effectively solving the problems, such as that raw material oil droplet jet velocity is too high makes catalyst breakage serious；Nozzle goes out
The arrangement of mouth may be configured as the various arrangement forms such as circular arrangement that is uniform, oval or limiting vertical direction width；Shower nozzle goes out
The surface at mouthful end is designed as the tangent plane that inclination angle is α in the horizontal direction, and α is 0-30 °, jet expansion center line in the horizontal direction with spray
Head axis angle is β, and β is 0-30 °；It is in fan-shaped to level two that arrangement above makes steam carry after feedstock oil is sprayed from jet expansion
Side is expanded, and forms broader steam screen, so that feedstock oil is fully reacted with catalyst.
The shower nozzle circumference of described multistage atomizing feed nozzle arranges multiple jet expansions, on spray outlet end face horizontal axis
The jet expansion of side is in Way out downward-sloping C1 angle；Outlet below spray outlet end face horizontal axis is in Way out
Upward deflect C2 angle；The outlet streams of diverse location are made to be pooled to flat area in reactor；Erect away from spray outlet end face
The corresponding different C1 and C2 numerical value of outlet of straight center line different distance.
In the jet expansion inner surface of shower nozzle or jet expansion contraction section inner surface or jet expansion contraction section and aditus laryngis section
Surface is set to many clover shapes, is preferentially set to bunge bedstraw herb shape, and this setting makes fourth stage atomization indirect steam that feedstock oil is rushed
Hit, breaking capacity higher.
Feedstock oil that is heated and having certain pressure enters mixed once spray chamber through raw material oil-in, and primary steam is through one
Secondary steam inlet enters primary steam room, and by the multiple primary steam spray orifice acceleration of circle distribution on primary steam orifice plate after
Enter mixed once spray chamber, feedstock oil carried out impact, crush, form first order atomization, simultaneously because primary steam orifice plate
The multiple steam fumaroles of upper circle distribution, around raw material oil-ins, form steamdrum and carry round feedstock oil and at a high speed feedstock oil
Flowing, reduces the gathering in side wall region for the big drop, strengthens atomizing effect；Primary steam carries feedstock oil and enters in inner tube, by
Tapered in the contraction section of inner tube, further through aditus laryngis section and expansion segment so that primary steam is to feedstock oil after circulation area contraction
Further impacted, crushed, make feedstock oil obtain second atomization, due to multigroup expansion segment, larynx can be arranged in inner tube
Mouth section and contraction section, make steam carry the multiple acceleration-deceleration of feedstock oil, now impact grinding ability is higher, and atomizing effect is more preferable；
Indirect steam enters indirect steam room through indirect steam entrance, and by the multiple secondary steaming of circle distribution on indirect steam orifice plate
Vapour spray orifice enters secondary mixed aerosol room after accelerating, with the feedstock oil flowing into secondary mixed aerosol room above by inner tube expansion segment
Mixing, is atomized further to it, even if feedstock oil obtains third time and is atomized；Indirect steam carries primary steam, feedstock oil enters
Jet expansion on shower nozzle, because jet expansion has contraction section, aditus laryngis section, circulation area is shunk and is made indirect steam in contraction section
Accelerate feedstock oil is further impacted, crush, form fourth stage atomization.Through level Four atomization, can effectively eliminate big
Diameter droplets are so that the feedstock oil entering riser reactor is fully contacted, reacts with catalyst, thus improving reaction yield.
Control due to each jet expansion direction has been carried out with design, carry out the expansion of β angle in the horizontal direction, enter in vertical direction
Row C1 and C2 angular direction flow to react outside spray outlet end and converge at atomization logistics jet length L of requirement, so that porous is flowed out
Oil and gas logistics formed in reactor flat distribution band, can sufficiently contact with the catalyst in reactor gasification, react.
C1 and C2 value is determined by L.
Multistage atomizing feed nozzle of the present utility model, compared with prior art, has following beneficial effect：
1st, the level Four atomization to feedstock oil can effectively eliminate major diameter drop, thus reaching required by catalytic cracking process
Atomizing particle size；
2nd, this jet expansion arrangement form makes steam carry after feedstock oil sprays and forms broader and flat steam oil gas
Screen, so that feedstock oil and catalyst are fully contacted, react, improves yield；
3rd, this jet expansion is provided with deceleration area, solves that raw material oil droplet jet velocity is too high to make catalyst breakage serious
Problem.
Brief description
Fig. 1-Figure 10 is multistage atomizing feed nozzle structure chart, specifically：
Fig. 1：Multistage atomizing feed nozzle structural representation；
Fig. 2：Inner tube 8 arranges the multistage atomizing feed nozzle structural representation of multigroup scaling section；
Fig. 3：The structural representation of A-A sectional view；
Fig. 4：The structural representation of B-B sectional view；
Fig. 5：Indirect steam spray orifice 10A is arranged on the multistage atomizing feed nozzle structural representation on inner tube 8 expansion segment 13；
Fig. 6-9：The schematic diagram of four kinds of structures of shower nozzle 12；
Figure 10：The structural representation of D-D sectional view.
In figure：1st, raw material oil-in, 2, primary steam entrance, 3, primary steam room, 4, primary steam orifice plate, 5, once mix
Close spray chamber, 6, indirect steam entrance, 7, outer tube, 8, inner tube, 9, secondary steam room, 10, indirect steam orifice plate, 11, secondary mixed
Close spray chamber, 12, shower nozzle, 13, expansion segment, 14, aditus laryngis section, 15, contraction section, 4A, primary steam spray orifice, 10A, indirect steam spray
Hole, 12A, jet expansion, 12B, jet expansion expansion segment, 12C, jet expansion aditus laryngis section, 12D, jet expansion contraction section, α, spray
Head port end surface horizontal direction angle of inclination, β, jet expansion center line horizontal direction angle, A1, inner tube expansion segment angle,
B1, internal tube shrinks section angle, A2, jet expansion expansion angle, B2, jet expansion converging angles, above C1, shower nozzle horizontal axis
Jet expansion vertical direction inclination angle, jet expansion vertical direction inclination angle below C2, shower nozzle horizontal axis, a, jet expansion erect
Nogata is to distributing position, b, jet expansion horizontal direction distributing position, the atomization logistics jet length that L, reaction require, φ 1, spray
Mouth exports throat diameter, φ 2, leafy grass diameter, φ 3, inner tube aditus laryngis section diameter.
Specific embodiment
With reference to the accompanying drawings and detailed description the utility model is described in further detail it is intended to help reader
Understand feature of the present utility model and essence, but the drawings and specific embodiments content is not intended to limit of the present utility model enforcement
Scope.
As shown in figure 1, a kind of multistage atomizing feed nozzle, described nozzle includes shower nozzle 12, outer tube 7, inner tube 8, feedstock oil
Entrance 1, primary steam entrance 2, primary steam orifice plate 4 and indirect steam entrance 6, indirect steam orifice plate 10；Described once
Steam orifice plate 4 is arranged between raw material oil-in 1 and inner tube 8, between primary steam orifice plate 4, raw material oil-in 1 and inner tube 8
Form toroidal cavity to constitute primary steam room 3 and arrange primary steam entrance 2, the downstream truncated cone-shaped region of primary steam orifice plate 4
Constitute mixed once spray chamber 5；Described indirect steam orifice plate 10 is arranged between inner tube 8 expansion segment 13 and outer tube 7, secondary
Form toroidal cavity between steam orifice plate 10, outer tube 7 and inner tube 8 and constitute indirect steam room 9, and in indirect steam orifice plate 10 logistics
Upstream arranges indirect steam entrance 6, and the concave regions between indirect steam orifice plate 10 and shower nozzle 12 and inner tube 8 outlet constitute secondary
Mixed aerosol room 11；Described inner tube 8 has mixed once spray chamber 5 and shrinkage expansion range of atomization, and shrinkage expansion range of atomization is again
Including expansion segment 13, aditus laryngis section 14 and contraction section 15；The described multiple primary steam spray orifice of primary steam orifice plate 4 circle distribution
4A, indirect steam orifice plate 10 circle distribution multiple indirect steam spray orifice 10A, shower nozzle 12 circle distribution multiple jet expansion 12A.
As shown in Fig. 2 the inner tube 8 of described multistage atomizing feed nozzle can have multiple shrinkage expansion ranges of atomization, that is, have
Multigroup expansion segment 13, aditus laryngis section 14 and contraction section 15, are 3 groups in this example.
As shown in Figure 3,4, the primary steam orifice plate 4 of above-mentioned multistage atomizing feed nozzle is around the circumference of raw material oil-in 1
The primary steam spray orifice 4A of M φ B of distribution, indirect steam orifice plate 10 is around the two of the N number of φ D of inner tube 8 expansion segment 13 circle distribution
Secondary steam fumarole 10A, M, N, B, D are determined by the treating capacity of feedstock oil, a pair of indirect steam spray orifice 10A and jet expansion 12A 1
Should, that is, number, orientation are all consistent.
As shown in figure 5, indirect steam spray orifice 10A can be located on inner tube 8 expansion segment 13.
As shown in Fig. 6,7,8, shower nozzle 12 circumference arranges multiple jet expansion 12A, and the structure setting of jet expansion 12A is
Wikipedia type, is made up of jet expansion contraction section 12D, jet expansion aditus laryngis section 12C, jet expansion expansion segment 12B, this structure can
So that feedstock oil obtains fourth stage atomization, form deceleration area in jet expansion expansion segment 12B simultaneously, effectively solve feedstock oil
Drip the too high problem making catalyst breakage serious of jet velocity；The arrangement of jet expansion 12A may be configured as circular uniform, oval
The various arrangement forms such as the arrangement of shape or restriction vertical direction width；The surface of shower nozzle 12 port of export is designed as in the horizontal direction
Steering angle be α tangent plane, α be 0-30 °, jet expansion 12A center line in the horizontal direction with shower nozzle axis angle be β, β be 0-
30°；It is in that sector is expanded to both sides that arrangement above makes steam carry feedstock oil from after jet expansion 12A ejection, is formed broader
Steam screen, so that feedstock oil is fully reacted with catalyst.
As shown in Figure 10, the jet expansion 12A above shower nozzle 12 exit end face horizontal axis deflects down in Way out
C1 angle；Jet expansion 12A below shower nozzle 12 exit end face horizontal axis upward deflects C2 angle in Way out；Make difference
The outlet streams of position are pooled to flat area in reactor；Away from going out of the shower nozzle 12 vertical center line different distance of exit end face
The different C1 and C2 numerical value of mouth correspondence.
As shown in figure 9, the jet expansion 12A inner surface of shower nozzle 12 or jet expansion contraction section 12D inner surface or nozzle go out
Mouth contraction section 12D and jet expansion aditus laryngis section 12C inner surface setting are many clover shapes, are preferentially set to bunge bedstraw herb shape, this setting
The fourth stage is made to be atomized indirect steam higher to the impact of feedstock oil, breaking capacity.In the application, described leafy grass is known car
Axle grass platymiscium, generally between three to 18, each blade presses axletree shaped formation to its blade, and bunge bedstraw herb shape presses Fig. 9
The quaterfoil clover shape of shown axletree shape arrangement.
Feedstock oil that is heated and having certain pressure enters mixed once spray chamber 5, primary steam warp through raw material oil-in 1
Primary steam entrance 2 enters primary steam room 3, and by the multiple primary steam spray orifice of circle distribution on primary steam orifice plate 4
4A enters mixed once spray chamber 5 after accelerating, and feedstock oil is carried out impact, crushes, and forms first order atomization, simultaneously because once
On steam orifice plate 4, multiple steam fumaroles 4A of circle distribution, around raw material oil-in 1, form steamdrum round feedstock oil simultaneously at a high speed
Carry feedstock oil flowing, reduce the gathering in side wall region for the big drop, strengthen atomizing effect；Primary steam carries feedstock oil and enters
Enter in inner tube 8, because the contraction section 15 of inner tube 8 is tapered, further through aditus laryngis section 14 and expansion segment 13 after circulation area contraction, make
Primary steam feedstock oil is further impacted, broken, make feedstock oil obtain second atomization, due to can in inner tube 8
To arrange multigroup expansion segment 13, aditus laryngis section 14 and contraction section 15, steam is made to carry the multiple acceleration-deceleration of feedstock oil, now impact cutting
Broken ability is higher, and atomizing effect is more preferable；Indirect steam enters indirect steam room 9 through indirect steam entrance 6, and passes through indirect steam
Indirect steam spray orifice 10A that on orifice plate 10, circle distribution is multiple enters secondary mixed aerosol room 11 after accelerating, and above by interior
Pipe 8 expansion segment 13 flows into the feedstock oil mixing of secondary mixed aerosol room 11, it is atomized further, even if feedstock oil obtains the 3rd
Secondary atomization；Indirect steam carry primary steam, feedstock oil enter shower nozzle 12 on jet expansion 12A, because jet expansion 12A has
Jet expansion contraction section 12D, jet expansion aditus laryngis section 12C, circulation area is shunk and is made indirect steam in jet expansion contraction section
12D accelerates feedstock oil is further impacted, crushes, and forms fourth stage atomization.Through level Four atomization, can effectively eliminate
Major diameter drop is so that the feedstock oil entering riser reactor is fully contacted, reacts with catalyst, thus improve reaction receiving
Rate.
Control due to each jet expansion 12A direction has been carried out with design, carry out the expansion of β angle in the horizontal direction, in vertically side
To carrying out C1 and C2 angular direction and flowing to react outside shower nozzle 12 port of export converging at atomization logistics jet length L of requirement, make many
The oil and gas logistics that hole is flowed out forms flat distribution band in reactor, sufficiently can contact gas with the catalyst in reactor
Change, react.C1 and C2 value is determined by L.
Embodiment
One nozzle feedstock oil inlet amount 25t/h, 250 DEG C of feeding temperature, feed pressure 0.7MPa（G）, reactor internal pressure
Power 0.2MPa（G）；Atomizing steam 1.0t/h, 250 DEG C of vapor (steam) temperature, steam pressure 0.8MPa（G）.
The utility model structure as shown in Figure 1, nozzle design example is as follows：
Oil-in 1 specification DN80, steam port 2 specification DN50, steam port 6 specification DN40, outer tube 7 internal diameter 132mm, inner tube 8
External diameter 89mm, φ 3=35mm, B1=20 °, A1=12 °, 4A number M=10, φ B=8mm, 10A number N=12, φ D=5mm, 12A number
Amount=12, φ 1=8mm, B2=15 °, A2=8 ° of α=β=15 °, C1=C2=5 °, L=400mm, steam port 2 quantity of steam 700kg/h, steam
Mouthful 6 quantity of steam 300kg/h, 12 12A circular arrangement as shown in Figure 6.
Claims (9)
1. a kind of multistage atomizing feed nozzle is it is characterised in that it includes shower nozzle（12）, outer tube（7）, inner tube（8）, feedstock oil enters
Mouthful（1）, primary steam entrance（2）, primary steam orifice plate（4）And indirect steam entrance（6）, indirect steam orifice plate（10）；Institute
The primary steam orifice plate stated（4）It is arranged on raw material oil-in（1）With inner tube（8）Between, in primary steam orifice plate（4）, feedstock oil
Entrance（1）And inner tube（8）Between formed toroidal cavity constitute primary steam room（3）And primary steam entrance is set（2）, once steam
Steam vent plate（4）Downstream side truncated cone-shaped region constitute mixed once spray chamber（5）；Said inner tube（8）Including mixed once mist
Change room（5）With shrinkage expansion range of atomization；Described indirect steam orifice plate（10）It is arranged on inner tube（8）Expansion segment（13）With outer tube
（7）Between, in indirect steam orifice plate（10）, outer tube（7）And inner tube（8）Between formed toroidal cavity constitute indirect steam room（9）,
And in indirect steam orifice plate（10）Logistics upstream arranges indirect steam entrance（6）, in indirect steam orifice plate（10）With shower nozzle（12）
And inner tube（8）Concave regions between outlet constitute secondary mixed aerosol room（11）；Described inner tube（8）There is expansion segment（13）、
Aditus laryngis section（14）, contraction section（15）；Described primary steam orifice plate（4）Circle distribution multiple primary steam spray orifice（4A）, secondary
Steam orifice plate（10）Circle distribution multiple indirect steam spray orifice（10A）, shower nozzle（12）The multiple jet expansion of circle distribution（12A）.
2. multistage atomizing feed nozzle as claimed in claim 1 is it is characterised in that inner tube（8）Shrinkage expansion range of atomization is by many
The process composition that individual flow cross gradually tapers up, expands, each contraction section（15）Angle B 1, expansion segment（13）Angle A 1 and each larynx
Mouth section（14）Diameter phi 3 designs as needed.
3. multistage atomizing feed nozzle as claimed in claim 1 is it is characterised in that the primary steam of multistage atomizing feed nozzle
Orifice plate（4）Around raw material oil-in（1）Circle distribution M φ B primary steam spray orifice（4A）, indirect steam orifice plate（10）Enclose
Around inner tube（8）Expansion segment（13）The indirect steam spray orifice of circle distribution N number of φ D（10A）, M, N, B, D are by the treating capacity of feedstock oil
Determine, indirect steam spray orifice（10A）With jet expansion（12A）Correspond, that is, number, orientation are all consistent.
4. multistage atomizing feed nozzle as claimed in claim 1 is it is characterised in that indirect steam spray orifice（10A）In being arranged on
Pipe（8）Expansion segment（13）On.
5. multistage atomizing feed nozzle as claimed in claim 1 is it is characterised in that shower nozzle（12）Circumference arranges multiple nozzles and goes out
Mouthful（12A）, jet expansion（12A）Structure setting be by jet expansion contraction section（12D）, jet expansion aditus laryngis section（12C）、
Jet expansion expansion segment（12B）Composition.
6. the multistage atomizing feed nozzle as described in claim 1 or 5 is it is characterised in that jet expansion（12A）Arrangement setting
For circular arrangement spread pattern that is uniform, oval or limiting vertical direction width.
7. multistage atomizing feed nozzle as claimed in claim 1 is it is characterised in that shower nozzle（12）The surface of the port of export is in level
Direction is designed as the tangent plane that inclination angle is α, and α is 0-30 °, jet expansion（12A）Center line in the horizontal direction with nozzle axis wire clamp
Angle is β, and β is 0-30 °.
8. multistage atomizing feed nozzle as claimed in claim 1 is it is characterised in that shower nozzle（12）On exit end face horizontal axis
The jet expansion of side（12A）Deflect down C1 angle in Way out；Shower nozzle（12）Nozzle below exit end face horizontal axis
Outlet（12A）Upward deflect C2 angle in Way out；The outlet streams of diverse location are made to be pooled to flat zone in reactor
Domain；Away from shower nozzle（12）The corresponding different C1 and C2 numerical value of the outlet of exit end face vertical center line different distance, C1 and C2 is by anti-
The atomization logistics jet length L value that should require determines.
9. multistage atomizing feed nozzle as claimed in claim 1 is it is characterised in that the jet expansion of shower nozzle (12)（12A）Interior
Surface or jet expansion contraction section（12D）Inner surface or jet expansion contraction section（12D）With jet expansion aditus laryngis section（12C）Interior table
Face is set to bunge bedstraw herb shape.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620645198.3U CN205953925U (en) | 2016-06-27 | 2016-06-27 | Multistage atomization feed nozzle |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620645198.3U CN205953925U (en) | 2016-06-27 | 2016-06-27 | Multistage atomization feed nozzle |
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| CN205953925U true CN205953925U (en) | 2017-02-15 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105950208A (en) * | 2016-06-27 | 2016-09-21 | 石宝珍 | Multistage-atomization feed nozzle |
-
2016
- 2016-06-27 CN CN201620645198.3U patent/CN205953925U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105950208A (en) * | 2016-06-27 | 2016-09-21 | 石宝珍 | Multistage-atomization feed nozzle |
| CN105950208B (en) * | 2016-06-27 | 2017-11-10 | 石宝珍 | A kind of multistage atomizing feed nozzle |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190927 Address after: 266555, No. 436, Wuyi Mountain Road, Qingdao economic and Technological Development Zone, Shandong, 10 Patentee after: QINGDAO JINGRUN PETROCHEMICAL ENGINEERING CO., LTD. Address before: 266400 Shandong city of Qingdao province Jiaonan City Road University Science Park of Qingdao Jingrun Petrochemical Design Institute Co. Ltd. Co-patentee before: Guo Wei Patentee before: Shi Bao Zhen |