CN218047940U - Chlorine dioxide preparation equipment - Google Patents
Chlorine dioxide preparation equipment Download PDFInfo
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- CN218047940U CN218047940U CN202221564941.4U CN202221564941U CN218047940U CN 218047940 U CN218047940 U CN 218047940U CN 202221564941 U CN202221564941 U CN 202221564941U CN 218047940 U CN218047940 U CN 218047940U
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- chlorine dioxide
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- raw material
- belt
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- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 title claims abstract description 230
- 238000002360 preparation method Methods 0.000 title claims abstract description 205
- 239000004155 Chlorine dioxide Substances 0.000 title claims abstract description 115
- 235000019398 chlorine dioxide Nutrition 0.000 title claims abstract description 115
- 239000002994 raw material Substances 0.000 claims abstract description 168
- 238000006243 chemical reaction Methods 0.000 claims abstract description 158
- 239000007788 liquid Substances 0.000 claims abstract description 84
- 238000010422 painting Methods 0.000 claims abstract description 21
- 230000007246 mechanism Effects 0.000 claims abstract description 19
- 238000002347 injection Methods 0.000 claims abstract description 17
- 239000007924 injection Substances 0.000 claims abstract description 17
- 239000003973 paint Substances 0.000 claims abstract description 6
- 239000007921 spray Substances 0.000 claims description 59
- 238000003860 storage Methods 0.000 claims description 49
- 238000004804 winding Methods 0.000 claims description 36
- 238000005507 spraying Methods 0.000 claims description 21
- 238000004519 manufacturing process Methods 0.000 claims description 19
- 238000010438 heat treatment Methods 0.000 claims description 11
- 230000001680 brushing effect Effects 0.000 claims description 4
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 238000005096 rolling process Methods 0.000 abstract description 11
- 241000243142 Porifera Species 0.000 description 41
- 239000000243 solution Substances 0.000 description 23
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 13
- 239000013589 supplement Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 9
- BZSXEZOLBIJVQK-UHFFFAOYSA-N 2-methylsulfonylbenzoic acid Chemical compound CS(=O)(=O)C1=CC=CC=C1C(O)=O BZSXEZOLBIJVQK-UHFFFAOYSA-N 0.000 description 8
- 239000002253 acid Substances 0.000 description 8
- 239000011550 stock solution Substances 0.000 description 7
- 230000008569 process Effects 0.000 description 6
- 239000011248 coating agent Substances 0.000 description 5
- 238000000576 coating method Methods 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 238000000889 atomisation Methods 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 4
- 238000004891 communication Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000003595 mist Substances 0.000 description 4
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 4
- 238000004659 sterilization and disinfection Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 230000003139 buffering effect Effects 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 235000010265 sodium sulphite Nutrition 0.000 description 2
- 241000195493 Cryptophyta Species 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 239000004696 Poly ether ether ketone Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 239000003899 bactericide agent Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920002530 polyetherether ketone Polymers 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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Abstract
The utility model provides a chlorine dioxide preparation equipment, chlorine dioxide preparation equipment includes the casing, receive and unreel unit, reaction area and first injection unit, be equipped with the gas vent on the casing, receive and unreel the unit and install in the casing, receive and unreel the unit including the rolling axle that carries out the rolling to the reaction area, unreel the axle and the rolling axle pivoted actuating mechanism that carry out the rolling to the reaction area, first injection unit is installed in holding the indoor, first injection unit includes first liquid reserve tank and installs the first shower nozzle on first liquid reserve tank, the jet of first shower nozzle is towards the area face setting of reaction area; the reaction zone is soaked with the first preparation raw material, or the chlorine dioxide preparation equipment further comprises a painting unit arranged in the containing chamber, and the painting unit paints the first preparation raw material on the surface of the zone. The chlorine dioxide preparation can make the preparation raw materials fully react, and can quickly, stably and reliably prepare the chlorine dioxide.
Description
Technical Field
The utility model relates to a chlorine dioxide preparation technical field, specifically speaking relates to a chlorine dioxide preparation equipment.
Background
Chlorine dioxide is a safe, broad-spectrum, high-efficiency and non-toxic bactericide, and can be widely applied to disinfection, sterilization, algae removal, oxidation treatment and the like. However, chlorine dioxide is difficult to store and transport due to its strong oxidizing property and easy decomposition, which causes inconvenience to some occasions requiring chlorine dioxide. Among them, for some industries requiring long-term and continuous use of chlorine dioxide, a stable and reliable chlorine dioxide device is needed to ensure the supply of chlorine dioxide; for example, the tap water industry requires the use of high purity chlorine dioxide for disinfection to reduce the harm to human body from the halogenated hydrocarbons currently produced by chlorine disinfection.
At present, the structure of the existing chlorine dioxide preparation equipment is generally complex, and the equipment cost is high; moreover, after the raw materials for preparing chlorine dioxide are synthesized into a solution in the preparation equipment, the solution concentration of the raw materials for preparing the chlorine dioxide with the optimal reaction effect is difficult to control, so that the phenomenon of incomplete reaction among the raw materials for preparing the chlorine dioxide is easy to occur, and further the waste of the raw materials for preparing the chlorine dioxide is caused.
Disclosure of Invention
In order to solve the above problems, it is a primary object of the present invention to provide a chlorine dioxide producing apparatus which can sufficiently react raw materials for production and can produce chlorine dioxide rapidly, stably and reliably.
In order to realize the main purpose of the utility model, the utility model provides a chlorine dioxide preparation device, wherein, including the casing, receive and release the reel unit, the reaction area, first injection unit and the control unit, the casing has the chamber, be provided with the gas vent on the casing, the gas vent communicates with the chamber, receive and release the reel unit and include the rolling axle, unreel axle and actuating mechanism, the rolling axle, unreel the axle and rotatably install in the chamber around the gyration axle center of self respectively, actuating mechanism drive rolling axle rotates, the reaction area winds respectively on rolling axle and unreeling axle, the rolling axle is to the reaction area rolling, unreel axle unreels to the reaction area, first injection unit installs in the chamber, first injection unit includes first liquid reserve tank and first shower nozzle, first shower nozzle installs on first liquid reserve tank, the jet of first shower nozzle sets up towards the band face of reaction area, the control unit is connected with actuating mechanism and first injection unit electricity respectively; the reaction zone is soaked with the first preparation raw material, or the chlorine dioxide preparation equipment further comprises a painting unit arranged in the containing chamber, the painting unit paints the first preparation raw material on the surface of the zone, and the painting unit is electrically connected with the control unit.
As can be seen from the above, the reaction zone is used to provide a reaction site for the preparation of chlorine dioxide, and the winding and unwinding unit is used to drive the reaction zone to move, so that the unreacted first preparation raw material on the reaction zone is mixed with the second preparation raw material sprayed by the first spraying unit on the reaction zone, when only two preparation raw materials are needed to prepare chlorine dioxide (such as sodium chlorate and hydrochloric acid, whose preparation chemical reaction formula is 2 NaClO) 3 +4HCl＝Cl 2 ↑+2ClO 2 ↑+2NaCl+2H 2 O), wherein the first preparation raw material on the reaction belt can be immersed into the reaction belt or coated on the belt surface of the reaction belt by a coating unit; and the prepared chlorine dioxide gas is discharged through the gas outlet and is sent to equipment to be used or an area to be used and the like. Through the design of the chlorine dioxide preparation equipment, the volume of the chlorine dioxide preparation equipment can be better reduced, the portability of the equipment is improved, and the contact area between the preparation raw materials can be increased, so that the equipment can be used for preparing chlorine dioxideThe raw materials are fully contacted, so that the chemical reaction is more thorough, and the raw materials for preparation are saved.
One preferred scheme is that the first nozzle comprises a first body and a heater, the first body is provided with a first liquid storage cavity, a first nozzle group communicated with the first liquid storage cavity is arranged on the first body, and the control unit can control the heater to heat the first liquid storage cavity.
It is thus clear that, when the second preparation raw materials in first liquid reserve tank enters into the first stock solution intracavity of first shower nozzle, the second preparation raw materials gasifies in the twinkling of an eye under the heating of heater, then utilize the pressure that its inflation produced to make the first nozzle group of second preparation raw materials spray to the area of reaction zone, make the degree of atomization of the second preparation raw materials that is erupted higher, with the area of contact of the first preparation raw materials on increase and the reaction zone, thereby make the reaction between the preparation raw materials more thorough, abundant, and avoid the waste of preparation raw materials.
Another preferred scheme is that the liquid storage box is provided with a liquid storage chamber and a buffer chamber, the liquid storage chamber is communicated with the buffer chamber, and the spray head is arranged at the bottom of the buffer chamber and is communicated with the buffer chamber.
It is thus clear that the stock solution room is used for saving the second and prepares the raw materials, and the setting of surge chamber is used for playing the cushioning effect to the second and prepares the raw materials, from making no matter how the liquid level and the hydraulic pressure of the second preparation raw materials in the surge chamber change, the hydraulic pressure of the inlet port department of first shower nozzle maintains at stable value always for the jet volumn of the second preparation raw materials that first shower nozzle erupted can keep the homogeneous state always.
It can be seen from above that, be provided with the sponge in the buffer chamber and can strengthen the buffering effect to second preparation raw materials to guarantee that first shower nozzle can spray second preparation raw materials uniformly.
Another preferred embodiment is that the height difference between the first spray head and the belt surface in the height direction of the housing is between 0.1 mm and 10 mm.
It is thus clear that above-mentioned design can guarantee that the second preparation raw materials that first shower nozzle erupted can be better fall on the area face in reaction area and cover the area face in reaction area to make the second preparation raw materials can carry out abundant contact, reaction with other preparation raw materials on the reaction area.
In another preferred embodiment, the chlorine dioxide producing apparatus further comprises at least one second spraying unit, the second spraying unit is installed in the containing chamber, the second spraying unit comprises a second liquid storage tank and a second spray head, the second spray head is installed on the second liquid storage tank, and the spray opening of the second spray head is arranged toward the strip surface.
From the above, when more than three preparation raw materials are needed for preparing chlorine dioxide, the other preparation raw materials can be sprayed one by one onto the belt surface of the reaction belt by adding at least one second spraying unit, so that all the preparation raw materials are subjected to chemical reaction on the reaction belt to produce chlorine dioxide.
Another preferred scheme is that a heating pipe is arranged in the shell and electrically connected with the control unit.
Therefore, the heating pipe can raise the temperature in the accommodating chamber, so that an excellent environment temperature is provided for the preparation of chlorine dioxide, and the reaction efficiency and effect of the preparation raw materials are improved.
The further scheme is that when chlorine dioxide equipment comprises a brushing unit, the brushing unit comprises a sponge roller shaft, the sponge roller shaft is rotatably arranged in the shell around the rotation axis of the sponge roller shaft, the sponge roller shaft is adjacent to the belt surface, and a first preparation raw material is soaked on the sponge roller shaft.
It can be seen from the above that when the unit is applied paint as to the sponge roller, the sponge roller can be on the area face of reaction zone with the first preparation raw materials roller coat that soaks on itself in the reaction zone course of marcing, simultaneously, the design can also be better reduce the volume of chlorine dioxide preparation equipment, improves the convenience of chlorine dioxide preparation equipment.
A sliding groove group is further arranged in the shell, sliding grooves of the sliding groove group extend towards the belt surface, and two ends of the sponge roller shaft are respectively connected with the sliding grooves of the sliding groove group in a sliding manner; the chlorine dioxide preparation equipment also comprises an elastic part, and the elastic part forces the sponge roller shaft to move towards the reaction belt along the chute; the sponge roller is located at the upstream end of the first spraying unit in the traveling direction of the reaction belt.
From top to bottom, can follow spout group through making the sponge roller and remove to set up the elastic component between sponge roller and casing, make the sponge roller can sticis on the reaction zone, and then guarantee that the sponge roller can advance the in-process with the reaction zone and go up the first preparation raw materials roller coat of soaking on self on the area of reaction zone, simultaneously, the volume that reduces chlorine dioxide preparation equipment that this design can also be better improves chlorine dioxide preparation equipment's convenience.
In another further scheme, when the chlorine dioxide equipment comprises the painting unit, the painting unit comprises a third liquid storage tank and a third spray head, the third spray head is arranged on the third liquid storage tank, and a spray opening of the third spray head faces the strip surface.
It can be seen from above that when adopting third liquid reserve tank and third shower nozzle as applying paint the unit with a brush, the third shower nozzle can advance the in-process at the reaction zone with the first preparation raw materials spraying in the third liquid reserve tank on the area face of reaction zone to make first preparation raw materials carry out abundant contact and carry out abundant chemical reaction with other preparation raw materials on the reaction zone.
Drawings
Fig. 1 is a schematic structural diagram of a first embodiment of the chlorine dioxide production apparatus of the present invention.
Fig. 2 is a schematic structural diagram of a first spray head of a first embodiment of the chlorine dioxide production apparatus of the present invention.
Fig. 3 is a schematic structural view of a first spray head of a second embodiment of the chlorine dioxide producing apparatus of the present invention.
Fig. 4 is a schematic structural view of a third embodiment of the chlorine dioxide producing apparatus of the present invention.
Fig. 5 is a schematic structural view of a fourth embodiment of the chlorine dioxide producing apparatus of the present invention.
FIG. 6 is a schematic structural view of a fifth embodiment of the chlorine dioxide producing apparatus of the present invention
Fig. 7 is a schematic structural view of a sixth embodiment of the chlorine dioxide producing apparatus of the present invention.
The present invention will be further described with reference to the accompanying drawings and examples.
Detailed Description
Chlorine dioxide production plant first embodiment
Referring to fig. 1 and 2, this embodiment will help to describe the chlorine dioxide production facility 100 of this embodiment by taking an example of using two production raw materials to perform a chemical reaction and further generate chlorine dioxide; wherein, the two preparation raw materials are hydrochloric acid solution (HCl, hereinafter referred to as "first preparation raw material") and sodium chlorate solution (NaClO) 3 Hereinafter referred to as "second preparation raw material"), the chemical reaction formula for preparing chlorine dioxide by using two preparation raw materials is: 2NaClO 3 +4HCl＝Cl 2 ↑+2ClO 2 ↑+2NaCl+2H 2 And O. The chlorine dioxide preparation equipment 100 comprises a shell 1, a winding and unwinding unit 2, a reaction belt 3, a first spraying unit 4, a painting unit 5 and a control unit 10.
The housing 1 preferably includes a third body 11 and a first cover 12, the third body 11 has a receiving chamber 111, and the first cover 12 is detachably mounted on the third body 11 and covers an opening of the receiving chamber 111 to seal the receiving chamber 111. The winding and unwinding unit 2, the reaction belt 3, the first spraying unit 4 and the painting unit 5 are all arranged in a containing chamber 111, the containing chamber 111 provides a space for preparing chlorine dioxide, and the first cover body 12 is matched to prevent generated chlorine dioxide gas from being directly dissipated in the air. Through the structural design of the shell 1, the winding and unwinding unit 2, the reaction belt 3, the first spraying unit 4 and the painting unit 5 are more convenient to disassemble, assemble and maintain. The third body 11 is provided with an exhaust port 112, the exhaust port 112 is communicated with the accommodating chamber 111, and the exhaust port 112 can be butted with a pipeline to deliver the generated chlorine dioxide gas to the equipment to be used or the area to be used. In addition, the third body 11 or the first cover 12 is preferably further provided with a first opening and a second opening, the first opening is provided with a second cover 12, so that the second cover 12 can open or close the first opening, and the second opening is provided with a third cover 12, so that the third cover 12 can open or close the second opening.
The winding and unwinding unit 2 comprises a winding shaft 21, an unwinding shaft 22, a tensioning wheel group 23 and a driving mechanism. The take-up reel is rotatably mounted in the housing chamber 111 around its own rotation axis, the pay-off reel 22 is rotatably mounted in the housing chamber 111 around its own rotation axis, and the take-up reel 21 is parallel to the pay-off reel 22. The reaction belt 3 is respectively wound on the winding shaft 21 and the unwinding shaft 22, the driving mechanism is installed in the accommodating chamber 111 and electrically connected with the control unit 10, and the driving mechanism is used for driving the winding shaft 21 to rotate, so that the winding shaft winds the reaction belt 3 wound thereon, and the unwinding shaft 22 unwinds the reaction belt 3 wound thereon, thereby enabling the reaction belt 3 to be kept in a tight state. Wherein, the reaction zone 3 provides a reaction site for the preparation of chlorine dioxide; preferably, the reaction tape 3 may be a thin tape made of nylon yarn, or may be an ink ribbon used in an ink jet printer.
The driving mechanism preferably adopts a direct current speed reducing motor, the working voltage of the direct current speed reducing motor is preferably between 3 volts and 12 volts, and the output rotating speed of the direct current motor is preferably between 600 revolutions per minute and 1200 revolutions per minute. It should be noted that, in other embodiments, the driving mechanism may also be: the winding device comprises a direct-current speed reducing motor, a first driving wheel, a second driving wheel and a driving belt, wherein the direct-current speed reducing motor is connected with a winding shaft 21 so as to drive the winding shaft 21 to rotate around a self rotation axis, the first driving wheel is connected with the winding shaft 21 and arranged coaxially with the winding shaft 21, the second driving wheel is connected with an unwinding shaft 22 and arranged coaxially with the unwinding shaft 22, and the driving belt is wound between the first driving wheel and the second driving wheel; the design of the driving mechanism enables the winding and unwinding unit 2 to drive the reaction belt 3 to transmit more stably and reliably. Of course, in other embodiments, the driving mechanism may drive the winding shaft 21, or the winding shaft 21 and the unwinding shaft 22 by a different connection manner or a different structure having the same function as the above-mentioned driving mechanism.
The tensioning unit comprises at least one tensioning roller shaft, and the tensioning roller shaft is used for being matched with the winding shaft 21, the unwinding shaft 22 or other tensioning roller shafts to ensure that the reaction belt 3 is always kept tight and simultaneously enable one part of the reaction belt 3 to be horizontally arranged. In the traveling direction of the reaction tape 3, the take-up roller shaft is located between the take-up shaft 21 and the pay-off shaft 22. As in the present embodiment, the number of the tension roller shafts is two, and two tension roller shafts are rotatably installed in the accommodating chamber 111 around their own axes, respectively, and are parallel to the take-up shaft 21, and the two tension roller shafts horizontally arrange the section of the reaction belt 3 astride therearound.
The first spraying unit 4 is installed in the accommodating chamber 111, and the first spraying unit 4 is located above the reaction zone 3 in the height direction of the housing 1. The first spray unit 4 includes a first liquid tank 41 and a first spray head 42, the first spray head 42 is installed on the first liquid tank 41, and a spray port of the first spray head 42 is disposed toward a belt surface of the reaction belt 3. Preferably, the height difference between the first nozzle 42 and the belt surface of the reaction belt 3 in the height direction of the casing 1 is between 0.1 mm and 10 mm, so as to ensure that the second preparation raw material sprayed by the first nozzle 42 can better fall on the belt surface of the reaction belt 3 and cover the belt surface of the reaction belt 3, thereby enabling the second preparation raw material to be in sufficient contact with and react with the second preparation raw material on the reaction belt 3.
Specifically, the first liquid storage tank 41 has a liquid storage chamber 411 and a buffer chamber 412, and the liquid storage chamber 411 is used for storing the second preparation raw material. A communication hole 414 is provided between the liquid storage chamber 411 and the buffer chamber 412, and the communication hole 414 communicates the liquid storage chamber 411 and the buffer chamber 412. Preferably, the communication hole 414 is provided near the bottom of the first tank 41 so that as much of the second preparation raw material as possible in the liquid storage chamber 411 can enter the buffer chamber 412 through the communication hole 414. The top of the liquid storage chamber 411 is provided with a first supplement port, and the first supplement port is communicated with the first opening through a first pipeline, so that a user can supplement the second preparation raw material into the liquid storage chamber 411 through the first opening, the first pipeline and the first supplement port.
A liquid outlet 4121 is arranged at the bottom of the buffer chamber 412; an air hole is formed in the upper portion of the buffer chamber 412, and the air hole communicates the buffer chamber 412 and the outside of the housing 1 through a pipe to balance the air pressure in the buffer chamber 412, so that the second preparation raw material in the buffer chamber 412 can flow out from the liquid outlet 4121. The buffer chamber 412 is configured to buffer the second preparation raw material, so that the liquid pressure at the liquid inlet 4212 of the first nozzle 42 is always maintained at a stable value no matter how the liquid level and the liquid pressure of the second preparation raw material in the buffer chamber 412 are changed, and the injection amount of the second preparation raw material injected by the first nozzle 42 can always be kept in a uniform state. Preferably, a screen is disposed on the air hole to prevent foreign materials from entering the buffer chamber 412 and contaminating the second preparation raw material and to prevent dust and particles from blocking the first nozzle 42. In addition, a sponge 413 is provided in the buffer chamber 412 to enhance the buffering effect on the second preparation raw material.
The first nozzle 42 includes a first body 421, a control chip and a heater 422, the control chip is electrically connected to the heater 422 and the control unit 10, respectively, so that when the control chip obtains a heating signal sent by the control unit 10, the heater 422 is controlled to generate heat according to a preset temperature according to the heating signal, and when the control chip obtains a heating stop signal sent by the control unit 10, the heater 422 is controlled to stop generating heat. A first liquid storage cavity 4211 is arranged in the first body 421, the first body 421 is installed on the first liquid storage tank 41 and is located below the buffer chamber 412, a liquid inlet 4212 is arranged on the first body 421, and the liquid inlet 4212 is butted and communicated with a liquid outlet 4121 of the buffer chamber 412, so that the second preparation raw material in the buffer chamber 412 can flow into the first liquid storage cavity 4211 through the liquid outlet 4121 and the liquid inlet 4212. In addition, a first nozzle group 4213 (i.e., the aforementioned injection ports) is disposed at the bottom of the first body 421, and the first nozzle group 4213 communicates with the first reservoir chamber 4211; wherein, the nozzles of the first nozzle set 4213 are all fine holes or micropores, so that the second preparation raw material can be sprayed out in the form of liquid drops, small liquid drops or atomization through the first nozzle set 4213.
The heater 422 is installed in the first reservoir 4211, or the heater 422 is installed in the first body 421 and located outside the first reservoir 4211 to heat the first reservoir 4211, or the heater 422 is installed in the first body 421 at the first nozzle group 4213 to heat the first nozzle group 4213. The heater 422 is used for heating the second preparation raw material in the first liquid storage cavity 4211, so that the second preparation raw material can be instantly gasified under the heating of the heater 422, and then the pressure generated by expansion of the second preparation raw material is utilized to enable the first nozzle group 4213 of the second preparation raw material to be sprayed to the belt surface of the reaction belt 3, so that the atomization degree of the sprayed second preparation raw material is higher, the contact area with the first preparation raw material on the reaction belt 3 is increased, so that the reaction between the preparation raw materials is more thorough and sufficient, and the waste of the preparation raw materials is avoided.
The applying brush unit 5 is installed in the accommodating chamber 111 and electrically connected to the control unit 10, and the applying brush unit 5 is used for applying the first preparation raw material to the belt surface of the reaction belt 3. In this embodiment, the applying brush unit 5 includes a third reservoir 51 and a third spray head 52, the third spray head 52 is installed at the bottom of the third reservoir 51, and the third spray head 52 is disposed toward the belt surface of the reaction belt 3. The applying brush unit 5 is located at an upstream end of the first spraying unit 4 in the traveling direction of the reaction belt 3. Preferably, the height difference between the third nozzle 52 and the belt surface of the reaction belt 3 in the height direction of the casing 1 is between 0.1 mm and 10 mm, so as to ensure that the first preparation raw material sprayed by the third nozzle 52 can better fall on the belt surface of the reaction belt 3 and cover the belt surface of the reaction belt 3, and thus the first preparation raw material can fully contact and react with the second preparation raw material on the reaction belt 3. The third liquid storage tank 51 has a single chamber, a second supplement port is arranged at the top of the third liquid storage tank 51, and the second supplement port is communicated with the second opening through a second pipeline, so that a user can supplement a second preparation raw material into the third liquid storage chamber 411 through the second opening, the second pipeline and the second supplement port; the third nozzle 52 is a common nozzle so that the first preparation raw material can be sprayed in the form of a fine liquid thread onto the belt surface of the reaction belt 3. Of course, in other embodiments, the third tank 51 may be configured the same as the first tank 41 and/or the third sprayer 52 may be configured the same as the first sprayer 42.
Preferably, a replacement window is provided on one side surface in the axial direction of the take-up shaft 21, and a seal door panel is provided on the replacement window so that the seal door panel can open or close the replacement window. Through setting up change window and sealing door board for the change of rolling axle 21, unreeling axle 22 and reaction area 3 is more convenient.
In addition, the acid solution (such as hydrochloric acid in this embodiment) in the preparation raw material is preferably industrial grade acid, the concentration of the acid solution is preferably between 16% and 20%, and the sodium chlorate solution is configured to be industrial grade 95%.
The preparation method of the chlorine dioxide preparing apparatus 100 of the present embodiment is briefly described as follows:
first, the concentrations of the first raw material for preparation [ e.g., an acid solution (e.g., a hydrochloric acid solution in this embodiment) ] and the second raw material for preparation (e.g., a sodium chlorate solution) are set, and the first raw material for preparation is added into the third liquid storage chamber 411 through the second opening, the second pipe and the second supplement port, and the second raw material for preparation is added into the liquid storage chamber 411 of the first liquid storage tank 41 through the first opening, the first pipe and the second supplement port.
Then, the control unit 10 controls the driving mechanism of the winding and unwinding unit 2 to drive the winding shaft 21 to wind the reaction tape 3, and the unwinding shaft 22 to unwind the reaction tape 3, so that the reaction tape 3 travels in the set traveling direction. In this process, the control unit 10 controls the third nozzle 52 of the painting unit 5 to start to paint the first preparation raw material on the surface of the reaction zone 3 passing through the third nozzle 52; and the control unit 10 controls the heater 422 of the first injection unit 4 to heat the second preparation raw material in the first reservoir 4211, so that the second preparation raw material is boiled and generates bubbles, so that the second preparation raw material is injected from the first nozzle group 4213 of the first spray head 42 through the bubbles, and the second preparation raw material is injected on the belt surface of the reaction belt 3 in a liquid mist shape, so that the first preparation raw material and the second preparation raw material are chemically reacted on the reaction belt 3 to produce chlorine dioxide gas.
The reaction belt 3 is continuously wound by the winding shaft 21, the reaction belt 3 is continuously unwound by the unwinding shaft 22, the first preparation raw material is continuously sprayed to the belt surface of the reaction belt 3 by the third spray head 52, the second preparation raw material is continuously sprayed to the belt surface of the reaction belt 3 by the first spray head 42, so that the first preparation raw material and the second preparation raw material are continuously subjected to chemical reaction, the generated chlorine dioxide gas is continuously increased, the air pressure in the accommodating chamber 111 of the shell 1 is continuously increased, and finally, the generated chlorine dioxide gas is discharged from the exhaust port 112 on the shell 1 to be conveyed to a device to be used or an area to be used for use.
Chlorine dioxide producing apparatus second embodiment
Referring to fig. 3, the present embodiment is different from the first embodiment of the chlorine dioxide producing apparatus in the structure of the first spray heads 6, specifically, in the present embodiment:
first shower nozzle 6 includes second body 61, diaphragm 62 and piezoelectric element 63, forms second stock solution chamber 611 between diaphragm 62 and the second body 61, is provided with second nozzle group 612 and inlet 613 with second stock solution chamber 611 intercommunication on the second body 61, inlet 613 docks, communicates with the outlet of the buffer chamber bottom of first stock solution case, piezoelectric element 63 borders on with diaphragm 62 and is located outside second stock solution chamber 611, but the extrusion diaphragm 62 of control unit 60 piezoelectric element 63 in to second stock solution chamber 611.
After the second preparation raw material in the first liquid storage tank enters the second liquid storage cavity 611 of the first spray head 6, when the control unit 60 controls the piezoelectric element 63 to deform, the piezoelectric element 63 can drive the diaphragm 62 adjacent to the piezoelectric element to deform together, so that the diaphragm 62 extrudes the second preparation raw material in the second liquid storage cavity 611, and further the second preparation raw material is ejected to the strip surface of the reaction zone through the second nozzle group 612, so as to more accurately control the size and the ejection direction of the droplets of the second preparation raw material, ensure the accurate control of the ejection of the second preparation raw material, and simultaneously, the atomization degree of the second preparation raw material ejected is higher, increase the contact area between the second preparation raw material and the first preparation raw material on the reaction zone, so that the reaction between the preparation raw materials is more thorough and sufficient, avoid the waste of the preparation raw materials, and can better reduce the energy consumption of the preparation equipment.
Chlorine dioxide production apparatus third embodiment
Referring to fig. 4, the present embodiment is different from the above embodiments in that:
in this embodiment, the setting of the applying brush unit is eliminated, and the reaction belt 64 is impregnated with the first preparation raw material.
The preparation method of the chlorine dioxide preparation facility of this example is briefly described as follows:
first, the concentrations of the first raw material for preparation [ e.g., an acid solution (hydrochloric acid solution in this example) ] and the second raw material for preparation (e.g., a sodium chlorate solution) are set. Placing the reaction zone 64 into the first preparation raw material to make the reaction zone 64 fully soaked with the first preparation raw material; a second preparation feedstock is added to the reservoir chamber of the first reservoir 68 through the first opening, the first conduit, and the second make-up port.
Then, the control unit controls the driving mechanism of the winding and unwinding unit to drive the winding shaft 65 to wind the reaction tape 64, and the unwinding shaft 66 to unwind the reaction tape 64, so that the reaction tape 64 travels in the set traveling direction. In the process, the control unit controls the first spray head 67 to work, so that the first spray head 67 sprays the second preparation raw material on the belt surface of the reaction belt 64 in a liquid mist shape, and the first preparation raw material and the second preparation raw material on the reaction belt 64 are subjected to chemical reaction to produce chlorine dioxide gas.
Wherein, as the winding shaft 65 continuously winds the reaction belt 64, the unwinding shaft 66 continuously unwinds the reaction belt 64, and the first nozzle continuously sprays the second preparation raw material to the belt surface of the reaction belt 64, so that the first preparation raw material and the second preparation raw material continuously perform chemical reaction, thereby continuously increasing the generated chlorine dioxide gas, continuously increasing the air pressure in the accommodating chamber 691 of the housing 69, and finally, the generated chlorine dioxide gas is discharged from the exhaust port 692 on the housing to be conveyed to the device to be used or the area to be used for use.
Fourth embodiment of chlorine dioxide production facility
Referring to fig. 5, the present embodiment is different from the first and second embodiments of the chlorine dioxide generating apparatus in the structure of the applying brush unit, specifically, in the present embodiment:
the coating unit comprises a sponge roller shaft 71, the sponge roller shaft 71 is rotatably arranged in a shell 72 around the rotation axis of the sponge roller shaft 71, the sponge roller shaft 71 is adjacent to the belt surface of the reaction belt 73, and the first preparation raw material is soaked on the sponge roller shaft 71. The sponge roller 71 is located at an upstream end of the first spraying unit 74 in the traveling direction of the reaction belt 73.
Preferably, a sliding groove group is further arranged in the housing 72, the sliding grooves of the sliding groove group extend towards the belt surface of the reaction belt 73, two ends of the sponge roller shaft 71 are respectively connected with the sliding grooves of the sliding groove group in a sliding manner, an elastic member is arranged between the sponge roller shaft 71 and the housing 72, and the elastic member forces the sponge roller shaft 71 to move towards the reaction belt 73 along the sliding grooves; as in the present embodiment, the chute extends along the belt surface of the reaction belt 73 in the height direction of the housing 72. Can follow the spout group through making sponge roller 71 remove to set up the elastic component between sponge roller 71 and casing 72, make sponge roller 71 can sticis on reaction area 73, and then guarantee that sponge roller 71 can be on reaction area 73 advances the in-process with the first preparation raw materials roller coat of self soaking on the area face of reaction area 73, simultaneously, the design can also be better reduce chlorine dioxide preparation equipment's volume, improve chlorine dioxide preparation equipment's convenience.
Wherein, the sponge layer of the sponge roller shaft 71 is made of acid-resistant plastic materials (such as polyetheretherketone, polytetrafluoroethylene, etc.), and the interior of the sponge layer is provided with a porous water absorption structure; of course, the sponge layer can be a water-absorbing consumable made of a rubber layer, silica gel or dead sponge. Preferably, the sponge roller 71 may be continuous for a period of between 240 hours and 360 hours.
The preparation method of the chlorine dioxide preparation facility of this example is briefly described as follows:
first, the concentrations of a first preparation raw material [ e.g., an acid solution (hydrochloric acid solution in this embodiment) ] and a second preparation raw material (e.g., a sodium chlorate solution) are configured, and the sponge roller 71 is put into the first preparation raw material, so that the sponge roller 71 is fully soaked with the first preparation raw material; a second preparation raw material is added into the liquid storage chamber of the first liquid storage tank 741 through the first opening, the first pipeline, and the second replenishment port.
Then, the control unit controls the driving mechanism of the winding and unwinding unit to drive the winding shaft 75 to wind the reaction tape 73, and the unwinding shaft 76 to unwind the reaction tape 73, so that the reaction tape 73 travels in the set traveling direction. In this process, the sponge roll 71 rolls the first preparation raw material impregnated thereon on the belt surface of the reaction belt 73 passing through the sponge roll 71; and the control unit controls the first spray head 67 to operate, so that the first spray head 67 sprays the second preparation raw material on the belt surface of the reaction belt 64 in a liquid mist shape, and the first preparation raw material and the second preparation raw material on the reaction belt 64 are subjected to chemical reaction to produce chlorine dioxide gas.
Wherein, as the winding shaft 75 continuously winds the reaction belt 73, the unwinding shaft 76 continuously unwinds the reaction belt 73, and the first nozzle 742 continuously sprays the second preparation raw material onto the belt surface of the reaction belt 73, so that the first preparation raw material and the second preparation raw material continuously perform chemical reaction, thereby continuously increasing the generated chlorine dioxide gas and increasing the air pressure in the accommodating chamber 721 of the housing 72, and finally, the generated chlorine dioxide gas is discharged from the exhaust port 722 on the housing 72 to be conveyed to the device to be used or the area to be used for use.
Fifth embodiment of chlorine dioxide production facility
Referring to fig. 6, the present embodiment is different from the above embodiments in that:
the chlorine dioxide producing apparatus further includes at least one second spraying unit 81, the second spraying unit 81 is installed in the receiving room 821 of the housing 82 and located above the parallel section of the reaction zone 83, the second spraying unit 81 includes a second liquid storage tank 811 and a second spray head 812, the second spray head 812 is installed on the second liquid storage tank 811, and a spray port of the second spray head 812 is disposed toward the zone surface. Of course, in other embodiments, the second reservoir 811 may be configured similar to the first reservoir 851 of the first spraying unit 85 and/or the second sprayer 812 may be configured similar to the first sprayer 852 of the first spraying unit 85. Preferably, the height difference between the second nozzle 812 and the belt surface of the reaction belt 83 in the height direction of the housing 82 is between 0.1 mm and 10 mm, so as to ensure that the third preparation raw material sprayed by the second nozzle 812 can better fall on the belt surface of the reaction belt 83 and cover the belt surface of the reaction belt 83, and thus the third preparation raw material can be in sufficient contact with and react with other preparation raw materials on the reaction belt 83.
It can be seen that, when more than three preparation raw materials are required for the preparation of chlorine dioxide, all the preparation raw materials may be chemically reacted on the reaction belt 83 by additionally providing at least one second injection unit 81 to inject the other preparation raw materials one by one onto the belt surface of the reaction belt 83, thereby producing chlorine dioxide.
For example, in the present example, the chemical reaction of three preparation raw materials to generate chlorine dioxide is taken as an example to assist the present exampleThe chlorine dioxide generating equipment of the examples is illustrated; wherein, the three preparation raw materials are respectively sulfuric acid solution (H) 2 SO 4 Hereinafter referred to as "first preparation raw material"), sodium chlorate solution (NaClO) 3 Hereinafter simply referred to as "second preparation raw material") and a catalyst or reducing agent solution [ e.g., sodium sulfite (Na) 2 SO 3 Hereinafter, it is abbreviated as "third preparation starting material"]The chemical reaction formula for preparing chlorine dioxide by adopting two preparation raw materials is as follows: 2NaClO 3 +Na 2 SO 3 +H 2 SO 4 ＝2ClO 2 ↑+2Na 2 SO 4 +H 2 And (O). The number of the second injection units 81 is one.
The preparation method of the chlorine dioxide preparation apparatus of this embodiment is briefly described as follows:
first, the concentrations of a first raw material for preparation [ e.g., an acid solution (sulfuric acid solution in this example) ], a second raw material for preparation (e.g., a sodium chlorate solution), and a third raw material for preparation (e.g., a sodium sulfite solution) ] are set; adding the first preparation raw material into the third liquid storage 861 of the painting unit 86 through the second opening, the second pipe and the second supplement port (when the painting unit 86 is not used, the application and addition manner of the first preparation raw material can refer to the third embodiment of the chlorine dioxide preparation apparatus, and when the painting unit 86 is used, the structure of the painting unit 86 is a sponge roller, the application and addition manner of the first preparation raw material can refer to the fourth embodiment of the chlorine dioxide preparation apparatus); adding a second preparation raw material into the liquid storage chamber of the first liquid storage tank 851 through the first opening, the first pipeline and the second supplement port; and adding a third preparation raw material into the liquid storage chamber of the second liquid storage tank 811, wherein the addition mode of the third preparation raw material can be set and added by referring to the addition modes of the first preparation raw material and the second preparation raw material.
Then, the control unit controls the driving mechanism of the winding/unwinding unit to drive the winding shaft 841 to wind the reaction tape 83, and the unwinding shaft 842 to unwind the reaction tape 83, so that the reaction tape 83 travels in the set traveling direction. In this process, the control unit controls the third sprayer 862 of the coating unit 86 to be activated to spray the first preparation raw material on the surface of the reaction belt 83 passing through the third sprayer 862 (when the coating unit 86 is not used, the manner in which the first preparation raw material is added to the reaction belt 83 may refer to the third embodiment of the chlorine dioxide preparation apparatus, and when the structure of the coating unit 86 is a sponge roller, the manner in which the first preparation raw material is added to the reaction belt 83 may refer to the fourth embodiment of the chlorine dioxide preparation apparatus); the control unit controls the second spray head 812 of the painting unit 86 to be started so as to spray the third preparation raw material on the strip surface of the reaction strip 83 passing through the second spray head 812; the control unit further operates the first showerhead 852 to spray the second preparation raw material onto the belt surface of the reaction belt 83 in a liquid mist form, and then to chemically react the first preparation raw material, the second preparation raw material, and the third preparation raw material on the reaction belt 83 to produce chlorine dioxide gas.
The first preparation raw material and the second preparation raw material are continuously chemically reacted by continuously spraying the third preparation raw material onto the belt surface of the reaction belt 83 through the second spray head 812 and the first spray head 852 onto the belt surface of the reaction belt 83, so that the generated chlorine dioxide gas is continuously increased and the air pressure in the accommodating chamber 821 of the housing 82 is continuously increased, and finally, the generated chlorine dioxide gas is discharged from the air outlet 822 of the housing 82 and is conveyed to the equipment to be used or the area to be used for use.
Sixth embodiment of chlorine dioxide producing apparatus
Referring to fig. 7, the present embodiment is different from the above embodiments in that:
in the present embodiment, the bottom of the housing 91 is provided with a discharge port 911, and the bottom wall of the accommodating chamber 910 is inclined, and the discharge port is located at the lower position of the inclined bottom wall, so that the liquid accumulated in the accommodating chamber 910 can be guided to the discharge port 911 by the inclined bottom wall, and further the liquid can be discharged from the discharge port 911 to the outside of the housing 91. Wherein, the discharge port 911 is provided with a valve 92, and the valve 92 can open or close the discharge port 911, so that the valve 92 can close the discharge port 911 to prevent the chlorine dioxide gas from being discharged from the discharge port 911 during the process of preparing chlorine dioxide; when it is necessary to clean the liquid accumulated in the containing chamber 910, the valve 92 is opened so that the liquid in the containing chamber 910 can be discharged out of the housing 91 through the discharge port 911.
Further, a pressure release valve 93 is arranged on the casing 91, so that when the exhaust port 912 of the casing 91 or a pipeline connected with the exhaust port 912 is blocked, the pressure release valve 93 can release pressure to the containing chamber 910 with continuously increased air pressure, so as to ensure safe use of the chlorine dioxide preparation equipment, and avoid explosion of the casing 91 caused by continuously increased pressure of the containing chamber 910.
Furthermore, a heating pipe 94 is disposed in the housing 91, and the heating pipe 94 can raise the temperature in the accommodating chamber 910, so as to provide an excellent environmental temperature for the preparation of chlorine dioxide, thereby improving the reaction efficiency and effect between the raw materials.
To sum up, the utility model provides a chlorine dioxide preparation equipment has the wide advantage of suitable scene, and its used spare part is little, and during the use, but reaction raw materials real-time allotment supplementary, very big liberation chlorine dioxide prepare the volume of system, improved the portability. In addition, through the design of the chlorine dioxide preparation equipment, the contact area between the preparation raw materials can be increased in the process of preparing chlorine dioxide, the preparation raw materials are fully contacted, the chemical reaction is more thorough, and the preparation raw materials are saved.
Finally, it should be emphasized that the above-described embodiments are merely preferred examples of the present invention, and are not intended to limit the invention, as those skilled in the art will appreciate that various changes and modifications may be made, and any and all modifications, equivalents, and improvements made, while remaining within the spirit and principles of the present invention, are intended to be included within the scope of the present invention.
Claims (10)
1. Chlorine dioxide production apparatus, characterized by comprising:
the reaction device comprises a shell, a winding and unwinding unit, a reaction belt, a first injection unit and a control unit, wherein the shell is provided with a containing chamber, an exhaust port is formed in the shell and communicated with the containing chamber, the winding and unwinding unit comprises a winding shaft, an unwinding shaft and a driving mechanism, the winding shaft and the unwinding shaft are respectively and rotatably installed in the containing chamber around a self rotating axis, the driving mechanism drives the winding shaft to rotate, the reaction belt is respectively wound on the winding shaft and the unwinding shaft, the winding shaft winds the reaction belt, the unwinding shaft unwinds the reaction belt, the first injection unit is installed in the containing chamber and comprises a first liquid storage tank and a first spray head, the first spray head is installed on the first liquid storage tank, a spray opening of the first spray head faces to the belt surface of the reaction belt, and the control unit is respectively and electrically connected with the driving mechanism and the first injection unit;
the reaction zone is impregnated with a first preparation raw material, or
The chlorine dioxide preparation equipment also comprises a painting unit arranged in the containing chamber, the painting unit paints the first preparation raw material on the surface of the strip, and the painting unit is electrically connected with the control unit.
2. The chlorine dioxide production facility of claim 1, wherein:
the first sprayer comprises a first body and a heater, the first body is provided with a first liquid storage cavity, a first nozzle group communicated with the first liquid storage cavity is arranged on the first body, and the control unit can control the heater to heat the first liquid storage cavity.
3. The chlorine dioxide production facility of claim 1, wherein:
the liquid reserve tank has liquid reserve room and buffer chamber, the liquid reserve room with the buffer chamber intercommunication, the shower nozzle sets up the buffer chamber bottom and with the buffer chamber intercommunication.
4. The chlorine dioxide production plant of claim 3, characterized in that:
the buffer chamber is internally provided with sponge.
5. The chlorine dioxide production facility of claim 1, wherein:
in the height direction of the shell, the height difference between the first spray head and the belt surface is between 0.1 mm and 10 mm.
6. The chlorine dioxide production facility of claim 1, wherein:
the chlorine dioxide preparation equipment also comprises at least one second injection unit, wherein the second injection unit is arranged in the containing chamber and comprises a second liquid storage tank and a second spray head, the second spray head is arranged on the second liquid storage tank, and a spray port of the second spray head faces the strip surface.
7. The chlorine dioxide production facility of claim 1, wherein:
and a heating pipe is arranged in the shell and is electrically connected with the control unit.
8. Chlorine dioxide production plant according to any one of claims 1 to 7, characterized in that:
when the chlorine dioxide equipment comprises the brushing unit, the brushing unit comprises a sponge roller shaft, the sponge roller shaft is rotatably arranged in the shell around the rotation axis of the sponge roller shaft, the sponge roller shaft is adjacent to the belt surface, and the first preparation raw material is soaked on the sponge roller shaft.
9. The chlorine dioxide production facility of claim 8, wherein:
a sliding groove group is further arranged in the shell, sliding grooves of the sliding groove group extend towards the belt surface, and two ends of the sponge roller shaft are respectively connected with the sliding grooves of the sliding groove group in a sliding manner;
the chlorine dioxide preparation equipment also comprises an elastic part, wherein the elastic part forces the sponge roller shaft to move towards the reaction belt along the chute;
the sponge roller is located at the upstream end of the first spraying unit in the traveling direction of the reaction belt.
10. Chlorine dioxide production plant according to any one of claims 1 to 7, characterized in that:
when the chlorine dioxide equipment comprises the painting unit, the painting unit comprises a third liquid storage tank and a third spray nozzle, the third spray nozzle is installed on the third liquid storage tank, and a spray port of the third spray nozzle faces the belt surface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221564941.4U CN218047940U (en) | 2022-06-20 | 2022-06-20 | Chlorine dioxide preparation equipment |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221564941.4U CN218047940U (en) | 2022-06-20 | 2022-06-20 | Chlorine dioxide preparation equipment |
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| CN218047940U true CN218047940U (en) | 2022-12-16 |
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| CN202221564941.4U Withdrawn - After Issue CN218047940U (en) | 2022-06-20 | 2022-06-20 | Chlorine dioxide preparation equipment |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114931924A (en) * | 2022-06-20 | 2022-08-23 | 珠海天威飞马打印耗材有限公司 | Chlorine dioxide preparation equipment and preparation method thereof |
| CN114984894A (en) * | 2022-06-20 | 2022-09-02 | 珠海天威飞马打印耗材有限公司 | Chlorine dioxide preparation equipment and preparation method thereof |
-
2022
- 2022-06-20 CN CN202221564941.4U patent/CN218047940U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114931924A (en) * | 2022-06-20 | 2022-08-23 | 珠海天威飞马打印耗材有限公司 | Chlorine dioxide preparation equipment and preparation method thereof |
| CN114984894A (en) * | 2022-06-20 | 2022-09-02 | 珠海天威飞马打印耗材有限公司 | Chlorine dioxide preparation equipment and preparation method thereof |
| CN114984894B (en) * | 2022-06-20 | 2024-07-12 | 珠海天威飞马打印耗材有限公司 | Chlorine dioxide preparation equipment and preparation method thereof |
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