CN205095763U - Spout - integral multiinjector structure of fluidized bed - Google Patents
Spout - integral multiinjector structure of fluidized bed Download PDFInfo
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- CN205095763U CN205095763U CN201520886451.XU CN201520886451U CN205095763U CN 205095763 U CN205095763 U CN 205095763U CN 201520886451 U CN201520886451 U CN 201520886451U CN 205095763 U CN205095763 U CN 205095763U
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- water conservancy
- conservancy diversion
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- spouted bed
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Abstract
The utility model discloses a spout - integral multiinjector structure of fluidized bed, air inlet nozzle are only one, and air inlet nozzle and spouting links together through the water conservancy diversion cover between the main part tip, a main part tip that spouts be straight tube section and taper pipe section, the water conservancy diversion cover divide into water conservancy diversion straight tube section and water conservancy diversion taper pipe section, the tip of water conservancy diversion straight tube section concreties in the straight tube section, straight tube section and the taper pipe duan shangjun processing of spouting a main part tip have a plurality of side wall hole cracks, from the air inlet nozzle get into gaseous partly direct get into spout a main part in, another part of gas of getting into from the air inlet nozzle gets into along the water conservancy diversion cover from the side wall hole crack spouts in the main part. To be used for the bypass nozzle of granule flow stateization to be in the same place with the whole design and processing of main burner, and distinguish gas injection to have extended to simultaneously and spout a lateral wall in annulus district, open the hole that has the some on the lateral wall, and can realize spouting 2 improvement of a granule, fluid two -phase flow process like this.
Description
Technical field
The utility model belongs to field of chemical equipment, relates to fluid bed, is specifically related to a kind of spraying-fluidized bed monoblock type multiinjector structure.
Background technology
Existing Pen Dong – fluid bed obtains common attention and the significant progress of spouted bed researcher and fluid bed researcher due to the advantage with spouted bed and fluid bed.This Pen Dong – fluid bed, compared with the spouted bed of routine, not only can promote the heat transfer between fluid and particle, mass transfer, can also effectively prevent from occurring dead band and the reunion of easy bonded particulate in annular space district bottom annular space district.But also Shortcomings part: maintain gas flow ratio needed for this Pen Dong – fluid bed separately spouted and needed for independent fluidisation throughput want large, 1. add certain bypass air feed auxiliary equipment simultaneously.2. the media particle in traditional spouted bed has significantly inside and outside laminar flow feature, and bed endoparticle lacks lateral/radial mixing, makes the surface of partial particulate fail acquisition and makes full use of, produce adverse influence to heat and mass in bed.
Summary of the invention
For the deficiencies in the prior art, the purpose of this utility model is, provides a kind of spraying-fluidized bed monoblock type multiinjector structure, improves while realizing spraying-fluidized bed particle and fluid two-phase flow process intensification technology.
In order to realize above-mentioned task, the utility model adopts following technical scheme to be achieved:
A spraying-fluidized bed monoblock type multiinjector structure, comprises spouted bed main body, and spouted bed body end is provided with inlet jet, and described inlet jet only has one, is linked together between inlet jet and spouted bed body end by flow guide sleeve;
Described spouted bed body end is divided into straight length and Taper Pipe section, and Taper Pipe section is near inlet jet;
Described flow guide sleeve is divided into water conservancy diversion straight length and deflection cone pipeline section, and the end of water conservancy diversion straight length is cemented on straight length;
Straight length and the Taper Pipe Duan Shangjun of described spouted bed body end are processed with multiple sidewall hole, the gas part entered from inlet jet directly enters in spouted bed main body, and the gas another part entered from inlet jet enters in spouted bed main body along flow guide sleeve from sidewall hole.
The utility model also has distinguishes technical characteristic as follows:
The shape of described sidewall hole is circular hole, and the diameter of circular hole is greater than the diameter of fluidized particle, and the diameter of circular hole is less than the internal diameter of inlet jet.
Annular space distance between the inwall of described water conservancy diversion straight length and the outer wall of straight length is 0.5 ~ 1 times of the internal diameter of inlet jet.
The length of described water conservancy diversion straight length is 1.1 times of the length of deflection cone pipeline section.
The tapering of described deflection cone pipeline section is 40 ° ~ 65 °, and the tapering of described Taper Pipe section equals the tapering of deflection cone pipeline section.
Compared with prior art, useful technique effect is the utility model:
Together with the bypass nozzle being used for particle fluidization is processed with main burner global design by the utility model, share same gas feed, gas inlet zone has been extended to the sidewall in spouted bed annular space district simultaneously, sidewall has the hole of some, 2 improvement of spouted bed particle, fluid two-phase mixtures process intensification can be realized like this.
Achieve the fluidization of spouted bed circular cone inclined-plane place particle, eliminate flow dead, bypass air feed equipment and associated pipe can be saved relative to the dynamic – fluidized-bed structure of spray simultaneously.
Compare and traditional spouted bed structure, hole place on annular space district sidewall has air-flow to inject, produce horizontal gas jet, thus realize the endocorpuscular fluidization in spouted bed annular space district, strengthen mixing of spouted bed annular space district endoparticle and inlet zone gas, spouted bed annular space district can be realized mix with the lateral/radial of gas in inlet zone and particle, thus the momentum of strengthening annular space district endoparticle and gas jet, heat and mass transfer process.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure, the implication of each label is: the spouted bed main body of 1-, 2-inlet jet, 3-flow guide sleeve, 4-sidewall hole; (1-1)-straight length, (1-2)-Taper Pipe section, (3-1)-water conservancy diversion straight length, (3-2)-deflection cone pipeline section.
Below in conjunction with drawings and Examples, particular content of the present utility model is described in more detail.
Detailed description of the invention
Defer to technique scheme, below provide specific embodiment of the utility model, it should be noted that the utility model is not limited to following specific embodiment, all equivalents done on technical scheme basis all fall into protection domain of the present utility model.Below in conjunction with embodiment, the utility model is described in further details.
Embodiment 1:
Defer to technique scheme, as shown in Figure 1, the present embodiment provides a kind of spraying-fluidized bed monoblock type multiinjector structure, comprise spouted bed main body 1, spouted bed main body 1 end is provided with inlet jet 2, described inlet jet 2 only has one, is linked together between inlet jet 2 and spouted bed main body 1 end by flow guide sleeve 3;
Described spouted bed main body 1 end is divided into straight length 1-1 and Taper Pipe section 1-2, and Taper Pipe section 1-2 is near inlet jet 2;
Described flow guide sleeve 3 is divided into water conservancy diversion straight length 3-1 and deflection cone pipeline section 3-2, and the end of water conservancy diversion straight length 3-1 is cemented on straight length 3-2;
The straight length 1-1 of described spouted bed main body 1 end and Taper Pipe section 1-2 is all processed with multiple sidewall hole 4, the gas part entered from inlet jet 2 directly enters in spouted bed main body 1, and the gas another part entered from inlet jet 2 enters in spouted bed main body 1 along flow guide sleeve 3 from sidewall hole 4.
The shape of sidewall hole 4 is circular hole, the diameter of circular hole is greater than the diameter of fluidized particle, the diameter of circular hole is less than the internal diameter of inlet jet 2, gas jet in sidewall circular hole can strengthen the local mixing of gas and particle in particle in spouted bed annular space district and inlet zone, strengthens the heat transfer in spouted bed, mass transport process.
Annular space distance between the inwall of water conservancy diversion straight length 3-1 and the outer wall of straight length 1-1 is 0.5 ~ 1 times of the internal diameter of inlet jet 2, thus ensures that gas jet enoughly can enter sidewall flow-guiding channel, and ensures certain gas jet velocity.
The length of water conservancy diversion straight length 3-1 is 1.1 times of the length of deflection cone pipeline section 3-2, thus ensures that flow-guiding channel outer wall gradient is consistent with spouted bed conical inboard wall gradient.
The tapering of deflection cone pipeline section 3-2 is 40 ° ~ 65 °, and the tapering of described Taper Pipe section 1-2 equals the tapering of deflection cone pipeline section 3-2, thus ensure that spouted bed can realize continuing, stable spouted.
Claims (5)
1. a spraying-fluidized bed monoblock type multiinjector structure, comprises spouted bed main body (1), and spouted bed main body (1) end is provided with inlet jet (2), it is characterized in that:
Described inlet jet (2) only has one, is linked together between inlet jet (2) and spouted bed main body (1) end by flow guide sleeve (3);
Described spouted bed main body (1) end is divided into straight length (1-1) and Taper Pipe section (1-2), and Taper Pipe section (1-2) is near inlet jet (2);
Described flow guide sleeve (3) is divided into water conservancy diversion straight length (3-1) and deflection cone pipeline section (3-2), and the end of water conservancy diversion straight length (3-1) is cemented on straight length (3-2);
The straight length (1-1) of described spouted bed main body (1) end and Taper Pipe section (1-2) are all processed with multiple sidewall hole (4), the gas part entered from inlet jet (2) directly enters in spouted bed main body (1), and the gas another part entered from inlet jet (2) enters in spouted bed main body (1) along flow guide sleeve (3) from sidewall hole (4).
2. monoblock type multiinjector structure spraying-fluidized bed as claimed in claim 1, it is characterized in that: the shape of described spouted bed main body wall hole (4) is circular hole, the diameter of circular hole is greater than the diameter of fluidized particle, and the diameter of circular hole is less than the internal diameter of inlet jet (2).
3. monoblock type multiinjector structure spraying-fluidized bed as claimed in claim 1, is characterized in that: the annular space distance between the inwall of described water conservancy diversion straight length (3-1) and the outer wall of straight length (1-1) is 0.5 ~ 1 times of inlet jet (2) internal diameter.
4. monoblock type multiinjector structure spraying-fluidized bed as claimed in claim 1, is characterized in that: the length of described water conservancy diversion straight length (3-1) is 1.1 times of the length of deflection cone pipeline section (3-2).
5. monoblock type multiinjector structure spraying-fluidized bed as claimed in claim 1, it is characterized in that: the tapering of described deflection cone pipeline section (3-2) is 40 ° ~ 65 °, the tapering of described Taper Pipe section (1-2) equals the tapering of deflection cone pipeline section (3-2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520886451.XU CN205095763U (en) | 2015-11-09 | 2015-11-09 | Spout - integral multiinjector structure of fluidized bed |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520886451.XU CN205095763U (en) | 2015-11-09 | 2015-11-09 | Spout - integral multiinjector structure of fluidized bed |
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| CN205095763U true CN205095763U (en) | 2016-03-23 |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109012514A (en) * | 2018-08-30 | 2018-12-18 | 亚洲硅业（青海）有限公司 | A kind of fluidized-bed reactor |
| CN109826710A (en) * | 2019-01-31 | 2019-05-31 | 西北工业大学 | Hyperbaric environment powder particle micro-disturbance starts fluidizer |
| CN111790321A (en) * | 2020-06-28 | 2020-10-20 | 西北大学 | Efficient-circulation uniform fluidizer and spouted bed |
| CN113941248A (en) * | 2021-11-24 | 2022-01-18 | 广州特种承压设备检测研究院 | Multi-nozzle spouted fluidized bed and simulation analysis method |
-
2015
- 2015-11-09 CN CN201520886451.XU patent/CN205095763U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109012514A (en) * | 2018-08-30 | 2018-12-18 | 亚洲硅业（青海）有限公司 | A kind of fluidized-bed reactor |
| CN109826710A (en) * | 2019-01-31 | 2019-05-31 | 西北工业大学 | Hyperbaric environment powder particle micro-disturbance starts fluidizer |
| CN111790321A (en) * | 2020-06-28 | 2020-10-20 | 西北大学 | Efficient-circulation uniform fluidizer and spouted bed |
| CN113941248A (en) * | 2021-11-24 | 2022-01-18 | 广州特种承压设备检测研究院 | Multi-nozzle spouted fluidized bed and simulation analysis method |
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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 |
Effective date of registration: 20200903 Address after: Room 2602, building 2, Xihe garden, 58 xihejia village, Beilin District, Xi'an City, Shaanxi Province Patentee after: Xi'an Mingbo Chemical Technology Co., Ltd Address before: 710069 Shaanxi city of Xi'an province Taibai Road No. 229 Patentee before: NORTHWESTERN University |
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| TR01 | Transfer of patent right |