CN109173625A - A kind of chemical industry temperature control dry chlorine device - Google Patents
A kind of chemical industry temperature control dry chlorine device Download PDFInfo
- Publication number
- CN109173625A CN109173625A CN201811207032.3A CN201811207032A CN109173625A CN 109173625 A CN109173625 A CN 109173625A CN 201811207032 A CN201811207032 A CN 201811207032A CN 109173625 A CN109173625 A CN 109173625A
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- CN
- China
- Prior art keywords
- pipe
- fixing pipe
- heat
- wall
- fixing
- 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
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- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 title claims abstract description 57
- 229910052801 chlorine Inorganic materials 0.000 title claims abstract description 57
- 239000000460 chlorine Substances 0.000 title claims abstract description 57
- 239000000126 substance Substances 0.000 title claims abstract description 22
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 73
- 238000002347 injection Methods 0.000 claims abstract description 39
- 239000007924 injection Substances 0.000 claims abstract description 39
- 239000006185 dispersion Substances 0.000 claims description 13
- 239000011148 porous material Substances 0.000 claims description 13
- 238000002156 mixing Methods 0.000 claims description 11
- 230000017525 heat dissipation Effects 0.000 claims description 8
- 230000004888 barrier function Effects 0.000 claims description 3
- 238000009826 distribution Methods 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 18
- 238000001035 drying Methods 0.000 abstract description 13
- 230000000694 effects Effects 0.000 abstract description 9
- 238000001816 cooling Methods 0.000 abstract description 5
- 238000011049 filling Methods 0.000 abstract description 4
- 238000000746 purification Methods 0.000 abstract description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000010992 reflux Methods 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- RHBGITBPARBDPH-ZPUQHVIOSA-N (E,E)-piperic acid Chemical compound OC(=O)\C=C\C=C\C1=CC=C2OCOC2=C1 RHBGITBPARBDPH-ZPUQHVIOSA-N 0.000 description 1
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
- B01D53/263—Drying gases or vapours by absorption
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
The invention discloses a kind of chemical industry temperature control dry chlorine devices, including the first fixing pipe and cool air hose, the side outer wall top position of first fixing pipe is sprue gated, and sulfuric acid injection pipe is plugged in inlet, first fixing pipe side inner wall top position is plugged with the first sealing-plug, and first is provided with gas outlet at the top of sealing-plug, escape pipe is plugged in the gas outlet, the side inner wall bottom position of first fixing pipe is equipped with third sealing-plug, and is provided with air inlet at the top of third sealing-plug.The chlorine of high temperature can be carried out heat transfer by the present invention, heat is adequately transmitted in the heat-conducting cylinder for filling dilute sulfuric acid, accelerate the volatilization of wherein water, dilute sulfuric acid is purified, it can promote the circulation of heat-conducting cylinder upper air, promote the volatilization of water in heat-conducting cylinder, improve the purification efficiency of dilute sulfuric acid, chlorine after cooling can be passed through in the first fixing pipe and be dried again, improve the drying effect of device.
Description
Technical field
The present invention relates to dry chlorine technical field more particularly to a kind of chemical industry temperature control dry chlorine devices.
Background technique
Currently, chlorine has many applications in the industrial production, such as bleaching agent, hydrochloric acid can be made etc., chlorine is producing
Certain moisture is often had in the process, if chlorine can react with water and generate time chlorine without being dried
Acid, then can cause to corrode to pipeline and equipment during pipeline transportation, present a large amount of chlorine drying methods mainly make
It is dried with some drying towers.
Through retrieving, Chinese patent grant number is the patent of CN205435412U, discloses a kind of novel chlorine drying device,
Including exhaust pipe, liquid feedstock valve, liquid feed pipe, liquid visor, intake valve, air inlet pipe, tapping valve, drain pipe, shell, row
Air valve, solids dryer, diffusing opening, liquid dryer, blowdown valve, sewage pipe and hang plate, the beneficial effects of the utility model
Be: hang plate makes filth-discharging effect good, is not in the case where sundries gets lodged in end-of-the-pipe, guarantees that sewage pipe has preferable stream
The general character.Moisture when dry in sulfuric acid absorption chlorine is had the disadvantage that in above-mentioned patent, generates a large amount of heat of dilution, it is dilute
Heat release is taken away by chlorine, is that the specific heat of chlorine is again small, temperature in drying tower certainly will be made to increase, drying tower exports chlorine temperature liter
Height, cause it is aqueous in chlorine increase, influence drying effect, and these heats can not utilize well, cause the wave of resource
Take.
Summary of the invention
The purpose of the present invention is to solve disadvantages existing in the prior art, and a kind of chemical industry temperature control chlorine proposed
Drying device.
To achieve the goals above, present invention employs following technical solutions:
A kind of chemical industry temperature control dry chlorine device, including the first fixing pipe and cool air hose, outside the side of first fixing pipe
Wall top position is sprue gated, and sulfuric acid injection pipe is plugged in inlet, position at the top of the inner wall of first fixing pipe side
It sets and is plugged with the first sealing-plug, and be provided with gas outlet at the top of the first sealing-plug, be plugged with escape pipe in the gas outlet, described
The side inner wall bottom position of one fixing pipe is equipped with third sealing-plug, and air inlet is provided at the top of third sealing-plug, and described the
The bottom of one fixing pipe has been bolted arc communicating pipe, and the other end of arc communicating pipe has been bolted second
Fixing pipe, second fixing pipe is equipped with residual heat using device far from the side outer wall of the first fixing pipe, and UTILIZATION OF VESIDUAL HEAT IN fills
It sets including heat-conducting cylinder, thermovent is provided at the top of the heat-conducting cylinder, the top position of second fixing pipe is plugged with the second sealing
Plug, and is provided with blow vent at the top of the second sealing-plug, be plugged with U-tube inside the blow vent, and the one of first fixing pipe
Observation window is provided on the outer wall of side, one end of the cool air hose is connected with air-cooler, and the other end of cool air hose is welded with main outlet air
Pipe.
As further scheme of the invention: the side outer wall bottom position of second fixing pipe is equipped with dispersion dress
It sets, and dispersal device includes fixed block, the intercommunicating pore equidistantly distributed is provided at the top of fixed block, the bore of intercommunicating pore bottom is big
Bore in top is welded with equidistant tilted-putted barrier bar on the inner wall of intercommunicating pore, passes through bolt at the top of fixed block
It is fixed with the dispersion mesh enclosure equidistantly distributed, dispersion mesh enclosure is respectively positioned on the top of intercommunicating pore.
As further scheme of the invention: being plugged with air inlet pipe, and air inlet pipe, outlet on the inner wall of the air inlet
Valve is equipped on pipe and sulfuric acid injection pipe.
As further scheme of the invention: being welded with mixing tube on the side outer wall of first fixing pipe, and mixed
It closes pipe to connect far from one end of the first fixing pipe with the second fixing pipe, height of the mixing tube close to first fixing pipe one end, which is lower than, to be leaned on
The height of nearly second fixing pipe one end.
As further scheme of the invention: being wrapped with thermally conductive endless tube, and thermally conductive endless tube on the outer wall of the heat-conducting cylinder
One end be connected with U-tube, the other end of thermally conductive endless tube is welded with the first connecting tube.
As further scheme of the invention: being bolted fixation on the side outer wall of second fixing pipe
Seat, and having heaters is bolted at the top of fixing seat.
As further scheme of the invention: the output end of the heater is connected with heat conducting bar, and heat conducting bar is located at
In heat-conducting cylinder.
As further scheme of the invention: the bottom of the heat-conducting cylinder has been bolted return pipe, and flows back
The other end of pipe is connect with the bottom of arc communicating pipe, and the first injection pipe and the second injection pipe are welded at the top of return pipe, the
The other end of one injection pipe is connected with the first fixing pipe, and the second injection pipe is located at close to the side of the second fixing pipe, the first note
The diameter for entering pipe is greater than the diameter of the second injection pipe, and the second injection pipe is arcuate structure.
As the present invention further scheme: the main discharge pipe is located at the surface of heat-conducting cylinder, and main discharge pipe
The secondary discharge pipe equidistantly distributed is welded on the outer wall of side.
As further scheme of the invention: being wrapped with heat dissipation on the outer wall of the cool air hose around pipe, and radiate around pipe
One end connect with the first connecting tube, the other end around pipe that radiates is connected with the second connecting tube, and the bottom of the second connecting tube with
The connection of first fixing pipe.
The invention has the benefit that
1. can disperse to chlorine bubbles by the setting of dispersal device interval bar and dispersion mesh enclosure, facilitate itself and dense sulphur
Acid is come into full contact with, and the drying efficiency of device is improved；
2. the setting by heat-conducting cylinder can collect dilute sulfuric acid, since the density of the concentrated sulfuric acid is greater than the density of water, so the concentrated sulfuric acid
The water generated after use can be moved in heat-conducting cylinder, the chlorine of high temperature can be carried out hot biography by the setting of thermally conductive endless tube
It leads, heat is adequately transmitted in the heat-conducting cylinder for filling dilute sulfuric acid, accelerate the volatilization of wherein water, dilute sulfuric acid is purified；
3. being utilized again by return line flow into arc communicating pipe, purified while taking full advantage of high temperature chlorine dilute
Sulfuric acid saves resource, can be the first fixing pipe of the concentrated sulfuric acid of reflux by the setting of the first injection pipe and the second injection pipe
In the second fixing pipe, and the second injection pipe arcuate structure, and the design close to the second fixing pipe side can be avoided chlorine
Gas enters in return pipe；
4. can heat to the dilute sulfuric acid in heat-conducting cylinder by the setting of heater and heat conducting bar, the volatilization of wherein water is improved
Efficiency can promote the circulation of heat-conducting cylinder upper air by the setting of secondary discharge pipe, promote the volatilization of water in heat-conducting cylinder, improve
The purification efficiency of dilute sulfuric acid；
5. by the setting of air-cooler can the air blast into cool air hose, cool down to the heat dissipation on its outer wall around pipe, thus right
Chlorine therein cools down, and avoids chlorine temperature high, influences drying effect；
It is dried, is improved again 6. the chlorine after cooling can be passed through in the first fixing pipe by the setting of the second connecting tube
The drying effect of device, enables to the sulphur in sulfuric acid and the second fixing pipe in the first fixing pipe by the setting of mixing tube
Acid is mixed, and avoids in two fixing pipes that sulfuric acid concentration gap is excessive, influences redrying effect.
It is not directed to part in the device to be the same as those in the prior art or can be realized by using the prior art, structure of the invention
Simply, easy to use, it can sufficiently dry, the heat in reasonable utilization chlorine, and solve chlorine to cross heat affecting dry
The problem of dry efficiency.
Detailed description of the invention
Fig. 1 is a kind of schematic cross-sectional view of chemical industry temperature control dry chlorine device proposed by the present invention；
Fig. 2 is a kind of local overlooking structural schematic diagram of chemical industry temperature control dry chlorine device proposed by the present invention；
Fig. 3 is a kind of residual heat using device side structure schematic view of chemical industry temperature control dry chlorine device proposed by the present invention；
Fig. 4 is a kind of residual heat using device overlooking structure diagram of chemical industry temperature control dry chlorine device proposed by the present invention；
Fig. 5 is a kind of dispersal device structural schematic diagram of chemical industry temperature control dry chlorine device proposed by the present invention.
In figure: 1 first fixing pipe, 2 first sealing-plugs, 3 escape pipes, 4 sulfuric acid injection pipes, 5 mixing tubes, 6 air inlet pipe, 7
Three sealing-plugs, 8 arc communicating pipes, 9 first injection pipes, 10 return pipes, 11 second injection pipes, 12 second fixing pipes, 13 dispersion dresses
It sets, 1303 intercommunicating pores, 1304 lattice bars, 1305 dispersion mesh enclosures, 14 fixing seats, 15 heaters, 16 heat conducting bars, 17 UTILIZATION OF VESIDUAL HEAT INs dress
It sets, 18 heat-conducting cylinders, 19 thermally conductive endless tubes, 20 first connecting tubes, 21 second sealing-plugs, 22 U-tubes, 23 main discharge pipes, 24 outlet air
Pipe, 25 cool air hoses, 26 heat dissipations are around pipe, 27 second connecting tubes, 28 air-coolers.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.
Referring to Fig.1-5, a kind of chemical industry temperature control dry chlorine device, including the first fixing pipe 1 and cool air hose 25, first is solid
The side outer wall top position for determining pipe 1 is sprue gated, and sulfuric acid injection pipe 4 is plugged in inlet, 1 side of the first fixing pipe
Inner wall top position is plugged with the first sealing-plug 2, and the top of the first sealing-plug 2 is provided with gas outlet, is plugged with outlet in gas outlet
The side inner wall bottom position of pipe 3, the first fixing pipe 1 is equipped with third sealing-plug 7, and the top of third sealing-plug 7 is provided with air inlet
Mouthful, the bottom of the first fixing pipe 1 has been bolted arc communicating pipe 8, and the other end of arc communicating pipe 8 is solid by bolt
Surely there is the second fixing pipe 12, the second fixing pipe 12 is equipped with residual heat using device 17 far from the side outer wall of the first fixing pipe 1, and
Residual heat using device 17 includes heat-conducting cylinder 18, and the top of heat-conducting cylinder 18 is provided with thermovent, the top position plug of the second fixing pipe 12
There is the second sealing-plug 21, and the top of the second sealing-plug 21 is provided with blow vent, U-tube 22 is plugged with inside blow vent, first is solid
Determine to be provided with observation window on the side outer wall of pipe 1, one end of cool air hose 25 is connected with air-cooler 28, and the other end weldering of cool air hose 25
It is connected to main discharge pipe 23.
In the present invention, the side outer wall bottom position of the second fixing pipe 12 is equipped with dispersal device 13, and dispersal device 13 wraps
Fixed block is included, the intercommunicating pore 1303 equidistantly distributed is provided at the top of fixed block, the bore of 1303 bottom of intercommunicating pore is greater than top
Bore, be welded with equidistant tilted-putted barrier bar 1304 on the inner wall of intercommunicating pore 1303, pass through spiral shell at the top of fixed block
Bolt is fixed with the dispersion mesh enclosure 1305 equidistantly distributed, and dispersion mesh enclosure 1305 is respectively positioned on the top of intercommunicating pore 1303, passes through dispersion
13 interval bar 1304 of device and dispersion mesh enclosure 1305 disperse chlorine bubbles, it is facilitated sufficiently to be connect with the concentrated sulfuric acid
Touching.
Wherein, it is plugged with air inlet pipe 6 on the inner wall of air inlet, and is all provided on air inlet pipe 6, escape pipe 3 and sulfuric acid injection pipe 4
There is valve.
Wherein, mixing tube 5 is welded on the side outer wall of the first fixing pipe 1, and mixing tube 5 is far from the first fixing pipe 1
One end is connect with the second fixing pipe 12, and height of the mixing tube 5 close to 1 one end of the first fixing pipe is lower than close to the second fixing pipe 12 1
The height at end is wrapped with thermally conductive endless tube 19 on the outer wall of heat-conducting cylinder 18, and one end of thermally conductive endless tube 19 is connected with U-tube 22,
The other end of thermally conductive endless tube 19 is welded with the first connecting tube 20, since the density of the concentrated sulfuric acid is greater than the density of water, so the concentrated sulfuric acid
The water generated after use can be moved in heat-conducting cylinder 18, the chlorine of high temperature be carried out heat transfer by thermally conductive endless tube 19, heat
Amount is adequately transmitted in the heat-conducting cylinder 18 for filling dilute sulfuric acid, is accelerated the volatilization of wherein water, is purified to dilute sulfuric acid, after purification
Sulfuric acid flow in arc communicating pipe 8 and utilized again by return pipe 10.
Wherein, fixing seat 14, and the top of fixing seat 14 have been bolted on the side outer wall of the second fixing pipe 12
It is bolted having heaters 15, the output end of heater 15 is connected with heat conducting bar 16, and heat conducting bar 16 is located at heat-conducting cylinder 18
It is interior, the dilute sulfuric acid in heat-conducting cylinder 18 is heated by heater 15 and heat conducting bar 16, the volatilization efficiency of wherein water is improved, leads
The bottom of hot cylinder 18 has been bolted return pipe 10, and the other end of return pipe 10 is connect with the bottom of arc communicating pipe 8,
The top of return pipe 10 is welded with the first injection pipe 9 and the second injection pipe 11, the other end and the first fixing pipe of the first injection pipe 9
1 is connected, and the second injection pipe 11 is located at close to the side of the second fixing pipe 12, and the diameter of the first injection pipe 9 is greater than the second injection
The diameter of pipe 11, the second injection pipe 11 is arcuate structure, by the first injection pipe 9 and the second injection pipe 11 the concentrated sulfuric acid of reflux
In first fixing pipe 1 and the second fixing pipe 12, and 11 arcuate structure of the second injection pipe, and close to 12 side of the second fixing pipe
Design can be avoided chlorine and enter in return pipe 10.
Wherein, main discharge pipe 23 is located at the surface of heat-conducting cylinder 18, and is welded on the side outer wall of main discharge pipe 23
The secondary discharge pipe 24 of range distribution is wrapped with heat dissipation on the outer wall of cool air hose 25 around pipe 26, and one end radiated around pipe 26 and the
The connection of one connecting tube 20, the other end around pipe 26 that radiates are connected with the second connecting tube 27, and the bottom of the second connecting tube 27 and the
The connection of one fixing pipe 1, by the air blast into cool air hose 25 of air-cooler 28, cools down to the heat dissipation on its outer wall around pipe 26, from
And cool down to chlorine therein, it avoids chlorine temperature high, influences drying effect, heat-conducting cylinder 18 is promoted by secondary discharge pipe 24
The circulation of upper air promotes the volatilization of water in heat-conducting cylinder 18, then the chlorine after cooling is passed through by the second connecting tube 27
It is dried again in first fixing pipe 1, improves the drying effect of device.
In use, chlorine was imported in arc communicating pipe 8 by air inlet pipe 6, then pass through 13 interval bar of dispersal device
1304 disperse chlorine bubbles with dispersion mesh enclosure 1305, facilitate it to be come into full contact with the concentrated sulfuric acid, due to the concentrated sulfuric acid
The density that density is greater than water passes through thermally conductive endless tube 19 so the water that the concentrated sulfuric acid generates after use can be moved in heat-conducting cylinder 18
The chlorine of high temperature is carried out heat transfer, heat is adequately transmitted in the heat-conducting cylinder 18 for filling dilute sulfuric acid, accelerates wherein water
Volatilization, purifies dilute sulfuric acid, and the sulfuric acid after purification is flowed in arc communicating pipe 8 by return pipe 10 and utilized again,
By the first injection pipe 9 and the second injection pipe 11 in the concentrated sulfuric acid the first fixing pipe 1 and the second fixing pipe 12 of reflux, Er Qie
Two injection pipes, 11 arcuate structure, and the design close to 12 side of the second fixing pipe can be avoided chlorine and enter in return pipe 10,
The dilute sulfuric acid in heat-conducting cylinder 18 is heated by heater 15 and heat conducting bar 16, the volatilization efficiency of wherein water is improved, passes through
The air blast into cool air hose 25 of air-cooler 28 cools down to the heat dissipation on its outer wall around pipe 26, to carry out to chlorine therein
Cooling avoids chlorine temperature high, promotes the circulation of 18 upper air of heat-conducting cylinder by secondary discharge pipe 24, promotes water in heat-conducting cylinder 18
Volatilization, then the chlorine after cooling is passed through in the first fixing pipe 1 by the second connecting tube 27 and is dried again, after dry
It is discharged and is collected by escape pipe 3, the sulfuric acid in sulfuric acid and the second fixing pipe 12 in the first fixing pipe 1 is made by mixing tube 5
It is mixed, avoids in two fixing pipes that sulfuric acid concentration gap is excessive, influence redrying effect.
The foregoing is only a preferred embodiment of the present invention, but scope of protection of the present invention is not limited thereto,
Anyone skilled in the art in the technical scope disclosed by the present invention, according to the technique and scheme of the present invention and its
Inventive concept is subject to equivalent substitution or change, should be covered by the protection scope of the present invention.
Claims (10)
1. a kind of chemical industry temperature control dry chlorine device, including the first fixing pipe (1) and cool air hose (25), which is characterized in that institute
The side outer wall top position for stating the first fixing pipe (1) is sprue gated, and sulfuric acid injection pipe (4), institute are plugged in inlet
It states the first fixing pipe (1) side inner wall top position to be plugged with the first sealing-plug (2), and is provided with out at the top of the first sealing-plug (2)
Port is plugged with escape pipe (3) in the gas outlet, and the side inner wall bottom position of first fixing pipe (1) is equipped with third
Sealing-plug (7), and air inlet is provided at the top of third sealing-plug (7), the bottom of first fixing pipe (1) is bolted
Have arc communicating pipe (8), and the other end of arc communicating pipe (8) has been bolted the second fixing pipe (12), described second
Fixing pipe (12) is equipped with residual heat using device (17) far from the side outer wall of the first fixing pipe (1), and residual heat using device
(17) include heat-conducting cylinder (18), thermovent, the top position of second fixing pipe (12) are provided at the top of the heat-conducting cylinder (18)
It sets and is plugged with the second sealing-plug (21), and be provided with blow vent at the top of the second sealing-plug (21), be plugged with U-shaped inside the blow vent
It manages (22), is provided with observation window on the side outer wall of first fixing pipe (1), one end of the cool air hose (25) is connected with cold wind
Machine (28), and the other end of cool air hose (25) is welded with main discharge pipe (23).
2. a kind of chemical industry according to claim 1 temperature control dry chlorine device, which is characterized in that second fixing pipe
(12) side outer wall bottom position is equipped with dispersal device (13), and dispersal device (13) includes fixed block, the top of fixed block
It is provided with the intercommunicating pore (1303) equidistantly distributed, the bore of intercommunicating pore (1303) bottom is greater than the bore at top, intercommunicating pore
(1303) it is welded with equidistant tilted-putted barrier bar (1304) on inner wall, has been bolted at the top of fixed block
The dispersion mesh enclosure (1305) of range distribution, dispersion mesh enclosure (1305) are respectively positioned on the top of intercommunicating pore (1303).
3. a kind of chemical industry according to claim 1 temperature control dry chlorine device, which is characterized in that the air inlet it is interior
It is plugged on wall air inlet pipe (6), and is equipped with valve on air inlet pipe (6), escape pipe (3) and sulfuric acid injection pipe (4).
4. a kind of chemical industry according to claim 1 temperature control dry chlorine device, which is characterized in that first fixing pipe
(1) it is welded on side outer wall mixing tube (5), and mixing tube (5) one end and the second fixing pipe far from the first fixing pipe (1)
(12) it connects, height of the mixing tube (5) close to the first fixing pipe (1) one end is lower than the height close to the second fixing pipe (12) one end
Degree.
5. a kind of chemical industry according to claim 1 temperature control dry chlorine device, which is characterized in that the heat-conducting cylinder (18)
Outer wall on be wrapped with thermally conductive endless tube (19), and one end of thermally conductive endless tube (19) is connected with U-tube (22), thermally conductive endless tube (19)
The other end be welded with the first connecting tube (20).
6. a kind of chemical industry according to claim 1 temperature control dry chlorine device, which is characterized in that second fixing pipe
(12) it has been bolted on side outer wall fixing seat (14), and has been bolted heating at the top of fixing seat (14)
Device (15).
7. a kind of chemical industry according to claim 6 temperature control dry chlorine device, which is characterized in that the heater (15)
Output end be connected with heat conducting bar (16), and heat conducting bar (16) is located in heat-conducting cylinder (18).
8. a kind of chemical industry according to claim 1 temperature control dry chlorine device, which is characterized in that the heat-conducting cylinder (18)
Bottom be bolted return pipe (10), and the other end of return pipe (10) is connect with the bottom of arc communicating pipe (8),
The first injection pipe (9) and the second injection pipe (11), the other end of the first injection pipe (9) and are welded at the top of return pipe (10)
One fixing pipe (1) is connected, and the second injection pipe (11) is located at close to the side of the second fixing pipe (12), the first injection pipe (9)
Diameter is greater than the diameter of the second injection pipe (11), and the second injection pipe (11) is arcuate structure.
9. a kind of chemical industry according to claim 1 temperature control dry chlorine device, which is characterized in that the main discharge pipe
(23) it is located at the surface of heat-conducting cylinder (18), and is welded with the secondary outlet air equidistantly distributed on the side outer wall of main discharge pipe (23)
It manages (24).
10. a kind of chemical industry according to claim 1 temperature control dry chlorine device, which is characterized in that the cool air hose
(25) heat dissipation is wrapped on outer wall around pipe (26), and heat dissipation is connect around one end of pipe (26) with the first connecting tube (20), is radiated
It is connected with the second connecting tube (27) around the other end of pipe (26), and the bottom of the second connecting tube (27) and the first fixing pipe (1) are even
It connects.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811207032.3A CN109173625B (en) | 2018-10-17 | 2018-10-17 | Chemical industry is with accuse temperature chlorine drying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811207032.3A CN109173625B (en) | 2018-10-17 | 2018-10-17 | Chemical industry is with accuse temperature chlorine drying device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109173625A true CN109173625A (en) | 2019-01-11 |
| CN109173625B CN109173625B (en) | 2021-03-26 |
Family
ID=64945482
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811207032.3A Active CN109173625B (en) | 2018-10-17 | 2018-10-17 | Chemical industry is with accuse temperature chlorine drying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109173625B (en) |
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| CN109173625B (en) | 2021-03-26 |
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