CN105478070A - Reaction tower with pneumatic stirring device - Google Patents
Reaction tower with pneumatic stirring device Download PDFInfo
- Publication number
- CN105478070A CN105478070A CN201510998672.0A CN201510998672A CN105478070A CN 105478070 A CN105478070 A CN 105478070A CN 201510998672 A CN201510998672 A CN 201510998672A CN 105478070 A CN105478070 A CN 105478070A
- Authority
- CN
- China
- Prior art keywords
- gas port
- blade
- main channel
- tower body
- described main
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 43
- 238000003756 stirring Methods 0.000 title abstract description 14
- 239000007921 spray Substances 0.000 claims description 27
- 230000002459 sustained effect Effects 0.000 claims description 4
- 230000004308 accommodation Effects 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 53
- 229920000642 polymer Polymers 0.000 description 18
- 239000002994 raw material Substances 0.000 description 17
- 230000000694 effects Effects 0.000 description 15
- 238000006116 polymerization reaction Methods 0.000 description 13
- 206010020852 Hypertonia Diseases 0.000 description 9
- 230000015572 biosynthetic process Effects 0.000 description 7
- 239000008234 soft water Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 229920002521 macromolecule Polymers 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000376 reactant Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000000178 monomer Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 230000033001 locomotion Effects 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 238000004880 explosion Methods 0.000 description 1
- 244000144992 flock Species 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/40—Mixers using gas or liquid agitation, e.g. with air supply tubes
- B01F33/402—Mixers using gas or liquid agitation, e.g. with air supply tubes comprising supplementary stirring elements
- B01F33/4021—Mixers using gas or liquid agitation, e.g. with air supply tubes comprising supplementary stirring elements the gas being introduced through the shaft of the stirring element
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/90—Heating or cooling systems
- B01F35/91—Heating or cooling systems using gas or liquid injected into the material, e.g. using liquefied carbon dioxide or steam
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/0066—Stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/2204—Mixing chemical components in generals in order to improve chemical treatment or reactions, independently from the specific application
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00121—Controlling the temperature by direct heating or cooling
- B01J2219/00123—Controlling the temperature by direct heating or cooling adding a temperature modifying medium to the reactants
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The invention relates to a reaction tower with a pneumatic stirring device, comprising a tower body and a stirring device, wherein the tower body is a cylinder and has a holding space; the stirring device comprises a rotary shaft which is arranged at the center position of the tower body along a vertical direction and capable of rotating under the driving of a power device and a plurality of paddles arranged on the rotary shaft at intervals along the axial direction of the vertical direction of the rotary shaft; the rotary shaft is hollow to form an air passage, main channels arranged along the axial directions of the paddles and lateral channels arranged by forming a certain angle with the main channels are formed in the paddles, the main channels are communicated with the air passage and extend towards the axial directions of the paddles to form main air nozzles, and the lateral channels are communicated with the main channels and extend towards the radial directions of the paddles to form lateral air nozzles.
Description
Technical field
The present invention relates to a kind of reaction tower with Pneumatic mixing device, belong to technical field of chemical.
Background technology
Macromolecular polymerization reaction joins in reaction vessel by each reactant feed, makes reaction monomers that polymerization formation high molecular polymer occur by controlling reaction condition.In order to enable reaction evenly carry out, need to stir the reactant in reaction vessel.At present, the churned mechanically mode of normal employing stirs reactant.
Chinese patent literature CN202778444U discloses the reaction vessel that a kind of Steam Heating stirs, and comprise tower body, be inserted into the pipeline of tower body inside, described pipeline has steam inlet.When specifically using, high steam enters into tower body inside by pipeline and the steam inlet be arranged on pipeline, to stir the liquefied mixture in tower body.But, because high steam directly passes into tower body inside by pipeline, thus the vapor stream of large stock is easily formed, and large stock vapor stream easily flocks together formation air pocket in liquefied mixture, air pocket once be formed and will float and overflow from the liquid level of liquefied mixture, thus causes the mixing effect of reactant undesirable in liquefied mixture.In addition, the bubble formed due to vapor stream is excessive, and the heat energy of steam has little time fully to exchange with liquefied mixture, steam cannot liquefy formation soft water completely, thus the quantity of steam in tower body can increase along with the increase passing into the time, can cause pressure increase in tower body, make tower body have the danger of blast; And in order to keep the stable of pressure in tower body, prevent pressure excessive, just the steam in tower body must be discharged, exhaust steam will reduce the utilization rate of steam, wastes the heat energy in steam and steam.
Summary of the invention
Therefore, technical problem to be solved by this invention is the problem that reaction vessel mixing effect is poor, steam utilization is low of prior art, thus provides the reaction tower that a kind of mixing effect is good, steam utilization is high.
For solving the problems of the technologies described above, the invention provides a kind of reaction tower with Pneumatic mixing device, comprising,
Tower body, for cylinder has spatial accommodation;
Agitating device, comprises the rotating shaft can rotated under power set drive vertically being arranged on described tower body center, and is arranged on the some blades in described rotating shaft along the axially spaced-apart of the vertical direction of described rotating shaft;
Described rotary shaft hollow forms air flue, described blade form along the axial arranged main channel of described blade, and form with described main channel the wing passage that certain angle arranges, described main channel is communicated with described air flue, and extending to form main jet gas port toward the axial direction of described blade, described wing passage is communicated with described main channel and the radial direction of past described blade extends to form side spray gas port;
The width of described air flue: the width of described main channel: the width of described wing passage=: 2-3: 1: 0.5-0.8; Vertical gap between described main jet gas port and the inwall of tower body is 80-100mm, and the distance of adjacent two described blade in the vertical directions is 400-600mm;
One end of described air flue is communicated with steam steam line, to make extraneous steam enter described air flue, sprays in described tower body finally by described main jet gas port and described side spray gas port;
The sidewall of described reaction tower arranges relief valve.
The angle formed between described main channel and horizontal plane is 3-4 °, described main channel horizontal-extending, and described wing passage is inclined on the sidewall of described main channel, and the angle that the axis of described wing passage and the axis of described main channel are formed is 8-15 °.
The diameter of described main jet gas port is 20-40mm, and the diameter of described side spray gas port is 10-20mm.
The diameter of described main channel becomes large from one end of main jet gas port gradually towards the one end be connected with described air flue, and the diameter of one end that described main channel is connected with described air flue is 1.30-1.40 times of described main jet gas port diameter.
Distance along adjacent two the described blade in the vertical directions of described rotating shaft vertical axis is 400-600mm, the diameter being positioned at described main jet gas port on the described blade of lower and described side spray gas port in two adjacent described blades be positioned at described main jet gas port on the described blade of eminence and described side spray gas port diameter 1.1-1.2 doubly.
Shape near the blade bottom described tower body is arc, has the vertical spout parallel with described shaft axis; The diameter of described vertical spout is 50-80mm.
In sustained height position, described rotating shaft connects two the described blades in left and right, the downward-sloping extension of described wing passage on blade described in side, the described wing passage on blade described in opposite side is inclined upwardly extension.
The other end of described air flue is provided with pressure limiting valve.
Technique scheme of the present invention has the following advantages compared to existing technology:
(1) reaction tower with Pneumatic mixing device of the present invention, agitating device and steam are passed into synthesis of mechanism integral, the rotating shaft and blade of agitating device form high-temperature steam circulation passage, high-temperature steam is from the puff prot ejection blade, because multiple blade and multiple puff prot are all positioned at tower body inside, the effect of dispersion steam can be played on the one hand, promote that steam liquefies at tower body, make steam with heat be fully discharged in tower body, the soft water as high molecular polymer raw materials for production is defined after steam liquefied, blade and puff prot also can follow axis of rotation on the other hand, steam is made to arrive each position in tower body more equably, improve the mixing effect of high-temperature steam to kettle inner macromolecule polymer raw material, make the reaction of high molecular polymer more abundant, evenly, unreacted polymerization single polymerization monomer content is low, and the molecular weight of high molecular polymer is comparatively even, and, the width of described air flue: the width of described main channel: the width of described wing passage=: 2-3: 1: 0.5-0.8, vertical gap between described main jet gas port and the inwall of tower body is 80-100mm, the distance of adjacent two described blade 22 in the vertical directions is 400-600mm, now, steam utilization up to the highest, and ensures that air pressure inside can not be too high and cause danger, by arranging side spray gas port and main jet gas port, high-temperature steam is made to have multiple jet direction, further increase the mixing effect of high-temperature steam, and enable high-temperature steam in high molecular polymerization raw material, be more prone to liquefaction formation soft water, prevent hypertonia in kettle.
(2) reaction tower with Pneumatic mixing device of the present invention, by arranging side spray gas port and main jet gas port, high-temperature steam is made to have multiple jet direction, further increase the mixing effect of high-temperature steam, and enable high-temperature steam in high molecular polymerization raw material, be more prone to liquefaction and form soft water, prevent hypertonia in kettle.
(3) reaction tower with Pneumatic mixing device of the present invention, described main channel horizontal-extending, described wing passage is inclined on the sidewall of described main channel, the angle that the axis of described wing passage and the axis of described main channel are formed is 8-15 °, thus make high-temperature steam have two component motions of upwards injection and horizontal-jet, make occurred level and the vertical stirring simultaneously of high molecular polymerization raw material, further increase stirring effect, and make high-temperature steam upwards impact high molecular polymerization raw material, drive high molecular polymer raw water is gentle to move both vertically, tower body 1 inner macromolecule polymer raw material is more even.
(4) reaction tower with Pneumatic mixing device of the present invention, because wing passage has shunted some vapor from main channel, reduce to prevent steam jet velocity, the diameter of main jet gas port is set to, than little 1.30-1.40 times of main channel inlets place, ensure the steam jet velocity from main jet gas port.
(5) reaction tower with Pneumatic mixing device of the present invention, distance along adjacent two the described blade in the vertical directions of described rotating shaft vertical axis is 400-600mm, described main jet gas port simultaneously on different blade and the diameter of described side spray gas port reduce gradually along with the increase of height, make jet amount also along with highly increasing and reduce, due to highly higher blade from liquid level more close to, the time of the stop of high-temperature steam in the high molecular polymer raw materials for production of liquid of the puff prot ejection on highly higher blade is shorter, thus in order to ensure that all high-temperature steams can liquefy completely, thus the increase of the diameter of main jet gas port described on different blade and described side spray gas port along with height is reduced gradually, to make full use of steam.
(6) reaction tower with Pneumatic mixing device of the present invention, shape near the blade bottom described tower body is arc, shape bottom blade laminating tower body is arranged, and vertical spout is set on blade, improve the stirring effect of the high molecular polymer bottom to tower body.
(7) reaction tower with Pneumatic mixing device of the present invention, in sustained height position, described rotating shaft connects two the described blades in left and right, the downward-sloping extension of described wing passage on blade described in side, the described wing passage on blade described in opposite side is inclined upwardly extension.Thus make upwards to spray, the amount of the gas of Jet with downward flow direction is roughly the same, thus ensures the consistent of reaction vessel interior pressure.
(8) reaction tower with Pneumatic mixing device of the present invention, the other end of described main channel is provided with pressure limiting valve.Pressure limiting valve is opened automatically when the hypertonia of main channel, releases portion gas, can prevent hypertonia in main channel and damage agitating device.
Accompanying drawing explanation
In order to make content of the present invention be more likely to be clearly understood, below according to a particular embodiment of the invention and by reference to the accompanying drawings, the present invention is further detailed explanation, wherein
Fig. 1 is the structural representation of the high molecular polymer reaction vessel of an embodiment of the present invention.
In figure, Reference numeral is expressed as: 1-tower body; 21-rotating shaft; 22-blade; The arc blade of 23-; 31-air flue; 32-main channel; 33-wing passage; The vertical spout of 34-.
Detailed description of the invention
Below in conjunction with accompanying drawing, technical scheme of the present invention is described in detail.
Embodiment 1
The present embodiment provides a kind of reaction tower with Pneumatic mixing device, as shown in Figure 1, comprises,
Tower body 1, for cylinder has spatial accommodation;
Agitating device, comprises the rotating shaft 21 can rotated under power set drive vertically being arranged on described tower body 1 center, and is arranged on the some blades 22 in described rotating shaft 21 along the axially spaced-apart of the vertical direction of described rotating shaft 21;
Described rotating shaft 21 hollow forms air flue 31, described blade 22 form along the axial arranged main channel 32 of described blade 22, and form with described main channel 32 wing passage 33 that certain angle arranges, described main channel 32 is communicated with described air flue 31, and extending to form main jet gas port toward the axial direction of described blade 22, described wing passage 33 is communicated with described main channel 32 and the radial direction of past described blade 22 extends to form side spray gas port;
The width of described air flue 31: the width of described main channel 32: the width of described wing passage 33=: 2-3: 1: 0.5-0.8; Vertical gap between described main jet gas port and the inwall of tower body 1 is 80-100mm, and the distance of adjacent two described blade 22 in the vertical directions is 400-600mm;
One end of described air flue 31 is communicated with steam steam line, to make extraneous steam enter described air flue 31, sprays in described tower body 1 finally by described main jet gas port and described side spray gas port;
The sidewall of described reaction tower arranges relief valve.
Above-mentioned have in the reaction tower of Pneumatic mixing device, agitating device and steam are passed into synthesis of mechanism integral, the rotating shaft 21 and blade 22 of agitating device form high-temperature steam circulation passage, high-temperature steam is from the puff prot ejection blade 4, because multiple blade 22 and multiple puff prot are all positioned at tower body 1 inside, the effect of dispersion steam can be played on the one hand, promote that steam liquefies at tower body 1, make steam with heat be fully discharged in tower body 1, the soft water as high molecular polymer raw materials for production is defined after steam liquefied, blade and puff prot also can follow axis of rotation on the other hand, steam is made to arrive each position in tower body more equably, improve the mixing effect of high-temperature steam to kettle inner macromolecule polymer raw material, make the reaction of high molecular polymer more abundant, evenly, unreacted polymerization single polymerization monomer content is low, and the molecular weight of high molecular polymer is comparatively even, and, the width of described air flue: the width of described main channel: the width of described wing passage=: 2-3: 1: 0.5-0.8, vertical gap between described main jet gas port and the inwall of tower body 1 is the distance of two described blade 22 in the vertical directions that 80-100mm is adjacent is 400-600mm, now, steam utilization up to the highest, and ensures that air pressure inside can not be too high and cause danger, by arranging side spray gas port and main jet gas port, high-temperature steam is made to have multiple jet direction, further increase the mixing effect of high-temperature steam, and enable high-temperature steam in high molecular polymerization raw material, be more prone to liquefaction formation soft water, prevent hypertonia in kettle 1.
Further, the angle formed between described main channel 32 and horizontal plane is 3-4 °, described main channel 32 horizontal-extending, described wing passage 33 is inclined on the sidewall of described main channel 32, the angle that the axis of described wing passage 33 and the axis of described main channel 32 are formed is 8-15 °, as 8 °, 10 °, 12 °, 15 ° etc.This kind of setting makes high-temperature steam have two component motions of upwards injection and horizontal-jet, make occurred level and the vertical stirring simultaneously of high molecular polymerization raw material, further increase stirring effect, and make high-temperature steam upwards impact high molecular polymerization raw material, drive high molecular polymer raw water is gentle to move both vertically, and tower body 1 inner macromolecule polymer raw material is more even; Further, main channel 32 and horizontal plane tilt certain angle a little, can ensure gas with having certain rotation direction from inflow side, main channel passage, have higher transition effect.
Further, the diameter of described main jet gas port is 20-40mm, and the diameter of described side spray gas port is 10-20mm.The diameter of described main channel 32 becomes large from one end of main jet gas port gradually towards the one end be connected with described air flue 31, the diameter of one end that described main channel 32 is connected with described air flue 31 is 1.30 times of described main jet gas port diameter, also can be the arbitrary value in 1.30-1.40 times, as 1.40 times.
Because wing passage 33 has shunted some vapor from main channel 32, in order to prevent steam jet velocity from reducing, the diameter of main jet gas port is set to, than little 1.30-1.40 times of porch, main channel 32, ensure the steam jet velocity from main jet gas port.
Further, distance along adjacent two the described blade in the vertical directions of described rotating shaft vertical axis is 400-600mm, as 400mm, 500mm, 600mm etc., the diameter being positioned at described main jet gas port on the described blade 22 of lower and described side spray gas port on adjacent two described blades 22 is 1.1 times of the diameter being positioned at described main jet gas port on the described blade 22 of eminence and described side spray gas port, also can be the arbitrary value in 1.1-1.2 times, as 1.2 times.
The distance of adjacent two described blade 22 in the vertical directions is 400-600mm, described main jet gas port simultaneously on different blade 22 and the diameter of described side spray gas port reduce gradually along with the increase of height, the jet amount made also reduces along with highly increasing, due to highly higher blade 22 from liquid level more close to, the time of the stop of high-temperature steam in the high molecular polymer raw materials for production of liquid of the puff prot ejection on highly higher blade 22 is shorter, thus in order to ensure that all high-temperature steams can liquefy completely, thus the increase of the diameter of main jet gas port described on different blade 22 and described side spray gas port along with height is reduced gradually, to make full use of steam.
Further, the shape near the blade 22 bottom described tower body 1 is arc, has the vertical spout with described rotating shaft 21 axis being parallel.Preferably, the diameter of described vertical spout is 75mm, and as distortion, described vertical spout also can be the arbitrary value in 50-80mm, as 50mm, 60mm, 70mm, 80mm etc.
Shape near the blade 22 bottom described tower body 1 is arc (being arc blade 23 in Fig. 1), the shape that blade 22 is fitted bottom tower body 1 is arranged, and vertical spout 34 is set on blade 22, improves the stirring effect of the high molecular polymer bottom to tower body 1.
Enter one not, in sustained height position, described rotating shaft 21 connects two the described blades 22 in left and right, the downward-sloping extension of described wing passage 33 on blade 22 described in side, the described wing passage 33 on blade 22 described in opposite side is inclined upwardly extension.Thus make upwards to spray, the amount of the gas of Jet with downward flow direction is roughly the same, thus ensures the consistent of reaction vessel interior pressure.
Further, the other end of described main channel 31 is provided with pressure limiting valve.
The other end of described main channel 31 is provided with pressure limiting valve.Pressure limiting valve is opened automatically when the hypertonia of main channel 31, releases portion gas, can prevent hypertonia in main channel 31 and damage agitating device.
Further, the sidewall of described reaction tower arranges relief valve, automatically open during the hypertonia of pressure limiting valve in reaction tower, release portion gas, hypertonia in reaction tower can be prevented and cause explosion danger.
Reaction tower described in above-described embodiment, is illustrated in figure 1 cylindrical shape, also can be other shape.
In order to keep temperature in kettle 1, the coil pipe arranged also can being set at tower body 1 outer wall, making kettle 1 temperature remained constant by passing into hot water in coil pipe around tower body 1.
What deserves to be explained is, for making high molecular weight reactive raw material enter in tower body 1, tower body 1 has charging aperture 12 for passing in tower body 1 for various raw material or other gas (as nitrogen) near top.
Obviously, above-described embodiment is only for clearly example being described, and the restriction not to embodiment.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here exhaustive without the need to also giving all embodiments.And thus the apparent change of extending out or variation be still among the protection domain of the invention.
Claims (8)
1. there is a reaction tower for Pneumatic mixing device, it is characterized in that, comprise,
Tower body (1), for cylinder has spatial accommodation;
Agitating device, comprise the rotating shaft (21) can rotated under power set drive vertically being arranged on described tower body (1) center, and be arranged on the some blades (22) in described rotating shaft (21) along the axially spaced-apart of the vertical direction of described rotating shaft (21);
It is characterized in that, described rotating shaft (21) hollow forms air flue (31), described blade (22) form along the axial arranged main channel (32) of described blade (22), and form with described main channel (32) wing passage (33) that certain angle arranges, described main channel (32) is communicated with described air flue (31), and extend to form main jet gas port toward the axial direction of described blade (22), described wing passage (33) is communicated with described main channel (32) and the radial direction of past described blade (22) extends to form side spray gas port,
The width of described air flue (31): the width of described main channel (32): the width of described wing passage (33)=: 2-3: 1: 0.5-0.8; Vertical gap between the inwall of described main jet gas port and tower body (1) is 80-100mm, and the distance of two adjacent described blade (22) in the vertical directions is 400-600mm;
One end of described air flue (31) is communicated with steam steam line, to make extraneous steam enter described air flue (31), sprays in described tower body (1) finally by described main jet gas port and described side spray gas port;
The sidewall of described reaction tower arranges relief valve.
2. the reaction tower with Pneumatic mixing device according to claim 1, it is characterized in that, the angle formed between described main channel (32) and horizontal plane is 3-4 °, described main channel (32) horizontal-extending, described wing passage (33) is inclined on the sidewall of described main channel (32), and the angle that the axis of described wing passage (33) and the axis of described main channel (32) are formed is 8-15 °.
3. the reaction tower with Pneumatic mixing device according to claim 1 and 2, is characterized in that, the diameter of described main jet gas port is 20-40mm, and the diameter of described side spray gas port is 10-20mm.
4. the reaction tower with Pneumatic mixing device according to claim 3, it is characterized in that, the diameter of described main channel (32) becomes large from one end of main jet gas port gradually towards the one end be connected with described air flue (31), and the diameter of one end that described main channel (32) are connected with described air flue (31) is 1.30-1.40 times of described main jet gas port diameter.
5. the reaction tower with Pneumatic mixing device according to claim 4, it is characterized in that, in two described blades (22) adjacent on described rotating shaft (21) vertical axis, the diameter being positioned at described main jet gas port on the described blade (22) of lower and described side spray gas port be positioned at described main jet gas port on the described blade (22) of eminence and described side spray gas port diameter 1.1-1.2 doubly.
6. the reaction tower with Pneumatic mixing device according to claim 5, it is characterized in that, shape near the blade (22) of described tower body (1) bottom is arc, has the vertical spout with described rotating shaft (21) axis being parallel; The diameter of described vertical spout is 50-80mm.
7. the reaction tower with Pneumatic mixing device according to any one of claim 1-6, it is characterized in that, in sustained height position, described rotating shaft (21) is upper connects two the described blades (22) in left and right, described wing passage (33) downward-sloping extension on blade described in side (22), the described wing passage (33) on blade described in opposite side (22) is inclined upwardly extension.
8. the reaction tower with Pneumatic mixing device according to any one of claim 1-7, is characterized in that, the other end of described air flue (31) is provided with pressure limiting valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510998672.0A CN105478070B (en) | 2015-12-28 | 2015-12-28 | A kind of reaction tower with Pneumatic mixing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510998672.0A CN105478070B (en) | 2015-12-28 | 2015-12-28 | A kind of reaction tower with Pneumatic mixing device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105478070A true CN105478070A (en) | 2016-04-13 |
| CN105478070B CN105478070B (en) | 2019-06-04 |
Family
ID=55665555
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510998672.0A Active CN105478070B (en) | 2015-12-28 | 2015-12-28 | A kind of reaction tower with Pneumatic mixing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105478070B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108424483A (en) * | 2018-06-05 | 2018-08-21 | 梁格 | A kind of polyethylene particles batch manufacturing method |
| CN108724517A (en) * | 2018-06-05 | 2018-11-02 | 梁格 | A kind of polyethylene particles production equipment |
| CN110743484A (en) * | 2019-12-11 | 2020-02-04 | 九江市美景水处理科技有限公司 | Intelligent reation kettle is used in polyaluminium chloride production |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002371102A (en) * | 2001-06-15 | 2002-12-26 | Mitsubishi Rayon Co Ltd | Method for polymerization of vintl monomer |
| CN202105611U (en) * | 2011-04-20 | 2012-01-11 | 江苏赛欧信越消泡剂有限公司 | Heating and mixing paddle of polymerization reactor |
| CN204429282U (en) * | 2015-01-22 | 2015-07-01 | 威海英卡瑞环保科技有限公司 | The spiral metal of polyacrylamide stirs cooling device |
| CN104923145A (en) * | 2015-06-30 | 2015-09-23 | 浙江天晨胶业股份有限公司 | Reaction container |
-
2015
- 2015-12-28 CN CN201510998672.0A patent/CN105478070B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002371102A (en) * | 2001-06-15 | 2002-12-26 | Mitsubishi Rayon Co Ltd | Method for polymerization of vintl monomer |
| CN202105611U (en) * | 2011-04-20 | 2012-01-11 | 江苏赛欧信越消泡剂有限公司 | Heating and mixing paddle of polymerization reactor |
| CN204429282U (en) * | 2015-01-22 | 2015-07-01 | 威海英卡瑞环保科技有限公司 | The spiral metal of polyacrylamide stirs cooling device |
| CN104923145A (en) * | 2015-06-30 | 2015-09-23 | 浙江天晨胶业股份有限公司 | Reaction container |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108424483A (en) * | 2018-06-05 | 2018-08-21 | 梁格 | A kind of polyethylene particles batch manufacturing method |
| CN108724517A (en) * | 2018-06-05 | 2018-11-02 | 梁格 | A kind of polyethylene particles production equipment |
| CN110743484A (en) * | 2019-12-11 | 2020-02-04 | 九江市美景水处理科技有限公司 | Intelligent reation kettle is used in polyaluminium chloride production |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105478070B (en) | 2019-06-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105457584A (en) | High-temperature reaction system | |
| CN105536675A (en) | Reaction device | |
| CN105478070A (en) | Reaction tower with pneumatic stirring device | |
| CN105080436A (en) | Ultrasonic coupling supergravity rotary packed bed and application thereof | |
| CN102358760A (en) | Stirred tank reactor | |
| CN105617968B (en) | A kind of device for collecting temperature control and stirring as one | |
| CN204874477U (en) | Solid -state distillation plant makes wine | |
| CN105413614A (en) | Uniform-pressure reaction tower | |
| CN103212346B (en) | Spouted bed reactor and olefin polymerization method thereof | |
| CN107051273B (en) | Environment-friendly compound feed preparation system | |
| CN209706526U (en) | Drying unit is used in agriculture fertilizer production | |
| CN105617938B (en) | A kind of high molecular polymer reaction vessel | |
| CN212017479U (en) | Nucleating agent production line | |
| CN205209136U (en) | Ferrous sulfate heptahydrate drying -machine | |
| CN205095662U (en) | Continuous solid body dissolving device | |
| CN105461841B (en) | The preparation method and propyl benzene latex of a kind of styrene-acrylic latex | |
| CN105642219A (en) | Blast-resistant reaction tower | |
| CN110217767A (en) | A kind of yellow phosphorus gasification combustion furnace | |
| CN215048842U (en) | High-temperature closed rotational flow air flotation floating oil collecting device | |
| CN206474058U (en) | A kind of urea for vehicle solution process units | |
| CN205517782U (en) | Automatic esterifying kettle of stirring | |
| CN209438582U (en) | A kind of preparation facilities of anti-chamotte mould polycarboxylate water-reducer | |
| CN108321426A (en) | A kind of preparation method and equipment of the nickel manganese cobalt acid lithium material of single-particle pattern | |
| CN202860551U (en) | Ion exchange device | |
| CN105831296A (en) | Energy-saving type tea leaf drying machine and tea leaf drying method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240320 Address after: 455100 Xijie Village, Yonghe Town, Anyang County, Anyang City, Henan Province Patentee after: Anyang Jinyukang Chemical Technology Co.,Ltd. Country or region after: Zhong Guo Address before: 325000 Binhai Park, Wenzhou Economic and Technological Development Zone, Zhejiang Province, 529, No. 15 Road, No. 2 Road Patentee before: Jin Ailian Country or region before: Zhong Guo |