CN114671153A - High-concentration hydrogen peroxide spraying cooling storage device circulating at high temperature in summer - Google Patents
High-concentration hydrogen peroxide spraying cooling storage device circulating at high temperature in summer Download PDFInfo
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- CN114671153A CN114671153A CN202210346246.9A CN202210346246A CN114671153A CN 114671153 A CN114671153 A CN 114671153A CN 202210346246 A CN202210346246 A CN 202210346246A CN 114671153 A CN114671153 A CN 114671153A
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- hydrogen peroxide
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- storage tank
- spray
- storage device
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- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 title claims abstract description 198
- 238000005507 spraying Methods 0.000 title claims abstract description 28
- 238000001816 cooling Methods 0.000 title claims abstract description 23
- 239000007921 spray Substances 0.000 claims abstract description 78
- 239000007788 liquid Substances 0.000 claims abstract description 75
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 60
- 238000011084 recovery Methods 0.000 claims description 19
- 241000237942 Conidae Species 0.000 claims description 7
- 210000005056 cell body Anatomy 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 5
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 229910000831 Steel Inorganic materials 0.000 description 15
- 239000010959 steel Substances 0.000 description 15
- 238000000354 decomposition reaction Methods 0.000 description 5
- 229910001220 stainless steel Inorganic materials 0.000 description 5
- 239000010935 stainless steel Substances 0.000 description 5
- 239000010865 sewage Substances 0.000 description 4
- 239000002826 coolant Substances 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 230000001502 supplementing effect Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 230000001680 brushing effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
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- 230000008569 process Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 230000008093 supporting effect Effects 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D88/00—Large containers
- B65D88/74—Large containers having means for heating, cooling, aerating or other conditioning of contents
- B65D88/744—Large containers having means for heating, cooling, aerating or other conditioning of contents heating or cooling through the walls or internal parts of the container, e.g. circulation of fluid inside the walls
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D90/00—Component parts, details or accessories for large containers
Abstract
The invention relates to a high-concentration hydrogen peroxide high-temperature circulating spray cooling storage device in summer, which comprises a hydrogen peroxide storage tank, a spray assembly, a deflection assembly and a liquid collecting tank, wherein the spray assembly, the deflection assembly and the liquid collecting tank are arranged outside the hydrogen peroxide storage tank, the top of the hydrogen peroxide storage tank is of a cone-shaped structure, the spray assembly is arranged at the top of the hydrogen peroxide storage tank, the deflection assembly is arranged at the bottom of the cone-shaped structure in a surrounding manner, the deflection assembly is connected with the hydrogen peroxide storage tank and has a distance, the liquid collecting tank is arranged at the bottom of the hydrogen peroxide storage tank, and the liquid collecting tank is connected with the hydrogen peroxide storage tank to form an annular tank body structure. Through spraying the cooling mode, can the effectual temperature in the control high concentration hydrogen peroxide solution storage tank, the effect is more obvious in summer, can prevent high temperature weather, and the high messenger jar internal hydrogen peroxide solution of storage tank temperature decomposes and brings the potential safety hazard, sprays still effectual water economy resource, economic environmental protection through the circulation.
Description
Technical Field
The invention belongs to the technical field of hydrogen peroxide storage, and particularly relates to a high-temperature circulating spraying cooling storage device for high-concentration hydrogen peroxide in summer.
Background
The information in this background section is only for enhancement of understanding of the general background of the invention and is not necessarily to be construed as an admission or any form of suggestion that this information forms the prior art that is already known to a person of ordinary skill in the art.
The high-concentration hydrogen peroxide has strong oxidizing property and instability, is transparent and colorless liquid at normal temperature, has pungent smell, has viscosity slightly larger than water, belongs to class A fire hazard dangerous goods, and is mainly characterized by combustion supporting property and easy decomposition to generate water and oxygen. The hydrogen peroxide is slowly decomposed at normal temperature to generate water and oxygen and simultaneously emit heat, the decomposition rate can be increased by 2.2 times when the temperature is increased by 10 ℃, so that the storage of high-concentration hydrogen peroxide has requirements on the temperature, the temperature is generally controlled below 30 ℃, and particularly, a storage tank needs to be protected when the hydrogen peroxide is stored in a high-temperature environment in summer. Most of the existing hydrogen peroxide storage tanks adopt a measure of brushing heat insulation paint on the tank body to ensure the temperature of the hydrogen peroxide in the storage tank, and although the measure can block partial atmospheric heat transfer and solar radiation heat, the temperature in the tank is still higher in the high-temperature period in summer.
Disclosure of Invention
In view of the problems in the prior art, the invention aims to provide a high-temperature circulating spraying cooling storage device for high-concentration hydrogen peroxide in summer.
In order to solve the technical problems, the technical scheme of the invention is as follows:
the utility model provides a high concentration hydrogen peroxide high temperature cycle sprays cooling storage device in summer, includes spray assembly, baffling subassembly, the collecting tank in hydrogen peroxide storage tank and the hydrogen peroxide storage tank outside, and the top of hydrogen peroxide storage tank is the tapered structure, and the spray assembly setting is at hydrogen peroxide storage tank top, and the baffling subassembly encircles the bottom that sets up at the tapered structure, be connected and have the interval between baffling subassembly and the hydrogen peroxide storage tank, the collecting tank setting is in the bottom of hydrogen peroxide storage tank, and the collecting tank is connected with the hydrogen peroxide storage tank and is formed annular cell body structure.
Adopt tank deck portion shower water, the shower water flows to tank body bottom along the jar body and retrieves, and the recovery water flows into the recovery pond, beats to the tank deck again through the pump and sprays the circulation and use, can effectually cool down to the jar body.
One or more technical schemes of the invention have the following beneficial effects:
the high-concentration hydrogen peroxide storage tank comprises a hydrogen peroxide storage tank, and a spray assembly, a baffling assembly and a liquid collecting tank which are arranged outside the hydrogen peroxide storage tank. The spraying assembly sprays out cooled liquid, the liquid flows along the outer side wall of the hydrogen peroxide storage tank through the baffling assembly, and then the liquid flows into the liquid collecting tank to be collected. Through spraying the cooling mode, can the effectual temperature in the control high concentration hydrogen peroxide solution storage tank, the effect is more obvious in summer, can prevent high temperature weather, and the high messenger jar internal hydrogen peroxide solution of storage tank temperature decomposes and brings the potential safety hazard, sprays still effectual water economy resource, economic environmental protection through the circulation.
Drawings
The accompanying drawings, which are incorporated in and constitute a part of this specification, are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification, illustrate exemplary embodiments of the invention and together with the description serve to explain the invention and not to limit the invention.
FIG. 1 is a diagram of an apparatus of a high concentration hydrogen peroxide circulating spray cooling system according to an embodiment of the present invention;
FIG. 2 is a schematic view of a sump structure according to an embodiment of the invention;
FIG. 3 is a schematic structural view of a spray assembly of an embodiment of the present invention;
FIG. 4 is a schematic view of the construction of a baffle assembly according to an embodiment of the present invention;
the device comprises a hydrogen peroxide storage tank, 2, a liquid collecting tank, 3, a spray water recovery water tank, 4, a spray water circulating pump, 5, a spraying component, 6, a baffling component, 7, a liquid collecting tank pouring valve, 8, a drainage valve, 9, a sewage tank valve, 10, a spraying valve, 11, a water supplementing valve, 2-1, a bottom ring plate, 2-2, a cylindrical plate, 2-3, outer ring angle steel, 2-4, inner ring angle steel, 2-5, a connecting pipe, 2-6, a flange, 5-1, a spraying pipe, 5-2, an overflow weir, 5-3, a connecting pipe and a flange, 6-1, a liquid receiving conical shell, 6-2, a rib plate, 6-3 and a baffle.
Detailed Description
It is to be understood that the following detailed description is exemplary and is intended to provide further explanation of the invention as claimed. Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this disclosure belongs.
It is noted that the terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of example embodiments according to the present disclosure. As used herein, the singular forms "a", "an" and "the" are intended to include the plural forms as well, and it should be understood that when the terms "comprises" and/or "comprising" are used in this specification, they specify the presence of stated features, steps, operations, devices, components, and/or combinations thereof, unless the context clearly indicates otherwise.
As shown in fig. 1, a high-concentration hydrogen peroxide spraying cooling storage device with high temperature circulation in summer, including spray assembly 5, baffling assembly 6, collecting tank 2 in hydrogen peroxide storage tank 1 and the hydrogen peroxide storage tank 1 outside, the top of hydrogen peroxide storage tank 1 is the taper type structure, and spray assembly 5 sets up at hydrogen peroxide storage tank 1 top, and baffling assembly 6 encircles the bottom that sets up at the taper type structure, be connected and have the interval between baffling assembly 6 and the hydrogen peroxide storage tank 1, collecting tank 2 sets up in the bottom of hydrogen peroxide storage tank 1, and collecting tank 2 is connected with hydrogen peroxide storage tank 1 and is formed annular cell body structure.
The invention relates to a high-temperature circulating spraying cooling storage device for hydrogen peroxide in summer, which is used for cooling a hydrogen peroxide storage tank to reduce the temperature of the hydrogen peroxide storage tank and reduce the decomposition of the hydrogen peroxide.
On hydrogen peroxide storage tank 1, from top to bottom spray assembly 5, baffling subassembly 6, collecting tank 2 in proper order, through spraying the spun coolant liquid, then the coolant liquid can flow along the outer wall of hydrogen peroxide storage tank under baffling subassembly's effect, is favorable to the cooling of hydrogen peroxide storage tank, then the coolant liquid enters into the collecting tank.
The top of the hydrogen peroxide storage tank 1 is of a conical structure, liquid sprayed by the spraying assembly flows downwards along the conical structure, most of the liquid flows outwards along the inclined plane of the cone when the liquid flows to the bottom of the conical structure, and the baffling assembly is arranged to block the liquid and enable the liquid to flow along the outer side wall of the hydrogen peroxide storage tank.
As a further technical scheme, the cross section of the hydrogen peroxide storage tank 1 is circular or square.
As a further technical scheme, the tank body at the bottom of the conical structure of the hydrogen peroxide storage tank 1 extends outwards to form a tank eave, and the tank eave is connected with the baffling assembly. The tank eave is favorable for fixing the baffling assembly, and baffling of liquid flow is realized at the position of the tank eave.
As shown in figure 4, as a further technical scheme, the baffling assembly comprises a baffle 6-3, rib plates 6-2 and a liquid-receiving conical shell 6-1, wherein the baffle 6-3 is of a cylindrical plate structure, the liquid-receiving conical shell is of a conical cylindrical plate structure, the rib plates 6-2 are of a V-shaped plate structure, the upper end of the liquid-receiving conical shell 6-1 is connected with the baffle 6-3, the lower end of the liquid-receiving conical shell is spaced from a hydrogen peroxide storage tank, a space is formed between the baffle and an eave, the V-shaped plate of the rib plates comprises a first rib plate and a second rib plate, the first rib plate is simultaneously connected with the eave and the liquid-receiving conical shell 6-1, and the end part of the second rib plate 6-2 is connected with the baffle 6-3.
As a further technical scheme, a plurality of rib plates 6-2 are arranged, and a space is arranged among the plurality of rib plates 6-2. Furthermore, the number of the rib plates 6-2 is 36-72, and the rib plates are evenly arranged along the circumferential direction of the top of the hydrogen peroxide storage tank at intervals.
The baffle, gusset, receive liquid cone shell to enclose into nearly rhombus's structure, the liquid that the toper structure of hydrogen peroxide storage tank flowed down flows to the tank eave through the interval between the gusset on, then falls to oblique below, then is blocked by the baffle, later vertical whereabouts, later flows towards the outer wall direction of hydrogen peroxide storage tank along receiving liquid cone shell slope again, then under the guide that receives liquid cone shell, flows to the hydrogen peroxide storage tank on, later along the vertical downward flow of hydrogen peroxide storage tank.
The gusset has the effect of connecting baffling subassembly and hydrogen peroxide storage tank, can have simultaneously and avoid a large amount of liquid that spray to cause great impact's effect to the baffle simultaneously. The spray liquid flows down through the position between the adjacent rib plates.
Further, the bottom end of the baffle 6-3 is positioned below the tank edge. Being provided with like this and doing benefit to and avoiding spraying liquid and tank eave to bump. Facilitating the flow of liquid down the baffle.
As a further technical scheme, the end part of the first rib plate penetrates through the tank edge and is connected with the liquid receiving conical shell. The position of the tank eave enables the spraying liquid to be buffered, then the flow direction is changed, and the rib plate penetrates through the tank eave to be arranged, so that the baffling component is fixed.
As a further technical scheme, the included angle between the liquid receiving conical shell and the baffle is 120-130 degrees, and the included angle between the baffle and the rib plate is 45-55 degrees. The angle is arranged to facilitate the change of the flow direction of the spraying liquid.
As a further technical solution, as shown in FIG. 3, the spray assembly 5 comprises a spray pipe 5-1 and an overflow weir 5-2, and the spray pipe 5-1 is positioned above the overflow weir 5-2. The overflow weir 5-2 can slow down the flowing speed of the spraying liquid, so that the top of the hydrogen peroxide storage tank is fully cooled.
As a further technical scheme, the spray pipe 5-1 is a circular ring-shaped pipe, and a plurality of spray holes are formed in the bottom of the spray pipe 5-1. The spray pipe is a circular ring pipe, which is beneficial to the uniform flow of liquid into the hydrogen peroxide storage tank.
As a further technical scheme, the overflow weir is a cylindrical plate, the bottom of the cylindrical plate is connected with the bottom of the hydrogen peroxide storage tank, and the top of the cylindrical plate is of a zigzag structure. Furthermore, the side length of the zigzag structure is 20-30mm, and the angle of the zigzag structure is 55-65 degrees.
As shown in figure 2, as a further technical scheme, the liquid collecting tank comprises a bottom ring plate 2-1 and a cylindrical plate 2-2, the bottom of the cylindrical plate 2-2 is connected with the bottom plate 2-1, the bottom ring plate is connected with the hydrogen peroxide storage tank, and the liquid collecting tank is formed among the bottom ring plate, the cylindrical plate and the hydrogen peroxide storage tank. Furthermore, outer ring angle steel 2-3 is arranged on the upper portion of the inner side wall of the liquid collecting tank, and inner ring angle steel 2-4 is arranged on the outer wall of the hydrogen peroxide storage tank and is opposite to the outer ring angle steel in position. Furthermore, the outer ring angle steel and the inner ring angle steel are respectively of an annular structure.
Further, the liquid collecting tank is spaced from the bottom surface of the hydrogen peroxide storage tank.
As a further technical scheme, the device also comprises a spray water recovery tank 3, wherein a water outlet of the liquid collecting tank 2 is connected with the spray water recovery tank 3, and an outlet of the spray water recovery tank is connected with a spray pipe 5-1.
Further, the bottom of the liquid collecting tank is provided with a liquid collecting tank inverse spraying valve 7 and a liquid collecting tank drainage valve 8, and the liquid collecting tank drainage valve 8 is arranged on a pipeline connected with the liquid collecting tank and the spray water recovery tank. Further, a water discharge valve 8 is arranged on a pipeline connecting a water outlet of the liquid collecting tank and the spray water recovery tank. The liquid collecting tank drainage valve 8 is arranged at the bottom of the liquid collecting tank 2 and used for discharging sundries in the liquid collecting tank 2 or discharging rainwater in the liquid collecting tank 2 in rainy days.
Further, a spray water circulating pump is arranged on a pipeline connecting an outlet of the spray water recovery tank with the spray pipe; a spray valve 10 is arranged on a pipeline connected with the outlet of the spray water circulating pump; the outlet of the spray water circulating pump is connected with a sewage pipeline, and a sewage pool valve 9 is arranged on the sewage pipeline. The spray water recovery tank is provided with a water replenishing pipeline, and a water replenishing valve 11 is arranged on the water replenishing pipeline.
Further, the spray water recovery tank is provided with a liquid level meter. And supplementing water when the liquid level of the spray water recovery water tank 3 is low. Further, a filter screen is arranged at the inlet of the spray water circulating pump; further, a filter screen is arranged at a water outlet of the liquid collecting tank. Preventing clogging. Furthermore, a pipeline for connecting the liquid collecting tank and the spray water recovery tank is a connecting pipe 2-5. The connecting pipe 2-5 is a bent pipe, is welded with the bottom of the bottom ring plate 2-1, and is welded with a filter screen at a pipe orifice connected with the bottom ring plate 2-1 for filtering impurities; flanges 2-6 are provided to connect to the nozzles 2-5 for connection to the valves.
The working principle is as follows:
the water is replenished to the liquid level of 80% through a water replenishing valve 11 of the spray water recovery tank 3, the spray water is pumped to a spray pipe 5-1 by a spray water circulating pump 4, the water is sprayed to the tank top through a round hole at the lower part of the spray pipe 5-1, the water flows downwards along the tank top and flows to an overflow weir 5-2, the water uniformly overflows to the middle lower part of the tank top from the upper part of the overflow weir 5-2, flows downwards along the tank top and flows to a liquid receiving conical shell 6-1 through a baffle 6-3, then uniformly flows downwards along the tank wall and flows to a liquid collecting tank 2, the water in the liquid collecting tank 2 flows back to the spray water recovery tank 3 through a liquid collecting tank drainage valve 8, and the spray water is recycled all the time.
The heat is taken away in the process that the spray water flows along the wall of the tank body, and meanwhile, a part of external heat can be isolated, so that the high-concentration hydrogen peroxide storage tank can be kept below 35 ℃ in a high-temperature environment in summer, the high-concentration hydrogen peroxide is prevented from rapidly rising in temperature and aggravating the decomposition of hydrogen peroxide in direct sunlight, and the potential safety hazard caused by decomposition of hydrogen peroxide in the high-temperature environment is solved; meanwhile, the spray water can be recycled, so that water resources are saved, the production cost of desalted water is reduced, and primary water and electric energy are indirectly saved.
Example 1
The specification of the hydrogen peroxide storage tank 1 is 6600mm in diameter, 8800mm in height, and the top of the tank is a conical storage tank.
The liquid collecting tank 2 comprises a bottom annular plate 2-1, a liquid collecting cylinder 2-2, outer ring angle steel 2-3, inner ring angle steel 2-4, a connecting pipe 2-5 and a flange 2-6, wherein the bottom annular plate 2-1 is welded with the high-concentration hydrogen peroxide storage tank 1, the height of the bottom annular plate is 4000mm higher than that of the high-concentration hydrogen peroxide storage tank 1, the bottom annular plate 2-1 is an annular plate with the thickness of 8mm, the diameter of the outer ring is 8016mm, and the diameter of the inner ring is 6850 mm; the liquid collecting cylinder 2-2 is a stainless steel cylinder with the equivalent diameter of 8000mm, the thickness of 8mm and the height of 450mm, and is vertically welded with the edge of the outer ring of the bottom ring plate 2-1; the outer ring angle steel 2-3 is angle steel with the width of 50mm multiplied by 5mm, and is welded with the upper edge of the liquid collecting cylinder 2-2; the inner ring angle steel 2-4 is angle steel with the width of 50mm multiplied by 5mm, and is welded on the outer cylinder body of the high-concentration hydrogen peroxide storage tank 1, and the height of the inner ring angle steel is the same as that of the outer ring angle steel 2-3; the connecting pipe 2-5 is a bent pipe with the diameter of 108 mm.
The spraying component 5 comprises a spraying pipe 5-1, an overflow weir 5-2, a connecting pipe and a flange 5-3, wherein the spraying pipe 5-1 is a cylindrical ring with the diameter of 89mm and the thickness of 4mm, the circumference is 3370mm, the spraying pipe 5-1 is welded with the tank top through 8 rib plates which are uniformly distributed on the circumference and are concentric with the tank top, and 220 circular holes with the diameter of 6mm are formed right below the spraying pipe 5-1 and are distributed on the circumference for spraying; the connecting pipe and the flange 5-3 are two paths of stainless steel pipes with the diameter of 57mm, are welded above the spray pipe 5-1 and are symmetrically distributed, and the connecting pipe and the flange 5-3 are connected with the spray water circulating pump 4 through a spray water pump outlet spray valve 10; the overflow weir 5-2 is a stainless steel cylinder with equivalent diameter 5400mm, thickness 4mm and height 100mm, the lower part of the overflow weir is welded on the tank top and is concentric with the tank top, the upper part of the overflow weir is triangular tooth-shaped, the side length is 25mm, the angle is 60 degrees, and the structure can enable water to uniformly flow downwards along the tank top.
The baffling component 6 comprises a baffle 6-3, the liquid receiving conical shell 6-1 and the baffle 6-3 are welded at an angle of 125 degrees and then welded to the eave edge of the tank top through a rib plate 6-2, the liquid receiving conical shell 6-1 is a stainless steel conical shell with the thickness of 4mm, the inner circle diameter of 6652mm, the outer circle diameter of 6840mm and the length of 120mm, and the inner circle and the gap are 10mm so as to flow water downwards; the baffle 6-3 is a stainless steel cylinder with an equivalent diameter of 6840mm, a thickness of 4mm and a height of 120mm, and is welded on the outer circle of the liquid receiving conical shell 6-1; the rib plates 6-2 are 12mm in thickness, 80mm in connection with the baffle plates 6-3, 73mm in connection with the high-concentration hydrogen peroxide storage tank 1 and 60mm in width, are close to rhombus, are connected with the high-concentration hydrogen peroxide storage tank 1, are provided with rectangular grooves with the length of 30mm, the height of 10mm and the upper edge difference of 10mm, and are used for being inserted into tank eaves, and the rib plates 6-2 are totally 78 and are evenly distributed on the tank eaves in a circumferential mode.
The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention, and various modifications and changes may be made by those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (10)
1. The utility model provides a high temperature circulation sprays cooling storage device in high concentration hydrogen peroxide summer which characterized in that: including spray set, baffling subassembly, the collecting tank in hydrogen peroxide storage tank and the hydrogen peroxide storage tank outside, the top of hydrogen peroxide storage tank is the taper type structure, and spray set sets up at hydrogen peroxide storage tank top, and the baffling subassembly encircles the bottom that sets up at the taper type structure, be connected and have the interval between baffling subassembly and the hydrogen peroxide storage tank, the collecting tank setting is in the bottom of hydrogen peroxide storage tank, and the collecting tank is connected with the hydrogen peroxide storage tank and is formed annular cell body structure.
2. The high-concentration hydrogen peroxide spray cooling storage device for high-temperature circulation in summer according to claim 1, characterized in that: the tank body of the conical structure bottom of the hydrogen peroxide storage tank extends outwards to form a tank eave, and the tank eave is connected with the baffling assembly.
3. The high-concentration hydrogen peroxide spray cooling storage device for high-temperature circulation in summer according to claim 1, characterized in that: the baffling subassembly includes baffle, gusset, receives liquid cone shell, the baffle is the drum plate structure, receives liquid cone shell for the cone type drum plate structure, and the gusset is V template structure, receives the upper end of liquid cone shell to be connected with the baffle, and the lower extreme sets up the interval with the hydrogen peroxide storage tank, has the interval between baffle and the eaves, and the V template of gusset includes first gusset and second gusset, and first gusset is connected with the eaves and receives liquid cone shell simultaneously, and the tip and the baffle of second gusset are connected.
4. The high-concentration hydrogen peroxide spray cooling storage device for high-temperature circulation in summer according to claim 3, characterized in that: the rib plates are provided with a plurality of ribs, and intervals are arranged among the plurality of rib plates.
5. The high-concentration hydrogen peroxide spray cooling storage device for high-temperature circulation in summer according to claim 3, characterized in that: the bottom end of the baffle is positioned below the tank brim.
6. The high-concentration hydrogen peroxide spray cooling storage device for high-temperature circulation in summer according to claim 3, characterized in that: the included angle between the liquid receiving conical shell and the baffle is 120-130 degrees, and the included angle between the baffle and the rib plate is 45-55 degrees.
7. The high-concentration hydrogen peroxide spray cooling storage device for high-temperature circulation in summer according to claim 1, characterized in that: the spraying assembly comprises a spraying pipe and an overflow weir, and the spraying pipe is positioned above the overflow weir.
8. The high-concentration hydrogen peroxide spray cooling storage device for high-temperature circulation in summer according to claim 7, characterized in that: the spray pipe is a circular ring pipe, and a plurality of spray holes are formed in the bottom of the spray pipe.
9. The high-concentration hydrogen peroxide spray cooling storage device for high-temperature circulation in summer according to claim 1, characterized in that: the liquid collecting tank comprises a bottom ring plate and a cylindrical plate, the bottom of the cylindrical plate is connected with the bottom plate, the bottom ring plate is connected with the hydrogen peroxide storage tank, and the liquid collecting tank is formed among the bottom ring plate, the cylindrical plate and the hydrogen peroxide storage tank.
10. The high-concentration hydrogen peroxide spray cooling storage device for high-temperature circulation in summer according to claim 7, characterized in that: the spray water recovery device further comprises a spray water recovery tank, the water outlet of the liquid collecting tank is connected with the spray water recovery tank, and the outlet of the spray water recovery tank is connected with the spray pipe.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202210346246.9A CN114671153A (en) | 2022-04-02 | 2022-04-02 | High-concentration hydrogen peroxide spraying cooling storage device circulating at high temperature in summer |
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| CN202210346246.9A CN114671153A (en) | 2022-04-02 | 2022-04-02 | High-concentration hydrogen peroxide spraying cooling storage device circulating at high temperature in summer |
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| CN209796376U (en) * | 2019-03-06 | 2019-12-17 | 无锡南泉压力容器有限公司 | Storage tank with spraying device |
| CN212830518U (en) * | 2020-05-08 | 2021-03-30 | 中国成达工程有限公司 | Fire-fighting cooling water diversion facility for storage tank and storage tank |
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2022
- 2022-04-02 CN CN202210346246.9A patent/CN114671153A/en active Pending
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|---|---|---|---|---|
| GB826742A (en) * | 1956-02-24 | 1960-01-20 | Georges Daric | Improvements in storage tanks |
| CN207078555U (en) * | 2017-07-06 | 2018-03-09 | 洛阳清源石化有限公司 | A kind of circulation type water-spraying heat sink of fuel oil drum |
| CN109422038A (en) * | 2017-09-01 | 2019-03-05 | 湖北恒泰新能源开发有限公司 | A kind of explosion-proof spray system of vertical methanol tank |
| CN109422032A (en) * | 2017-09-01 | 2019-03-05 | 湖北恒泰新能源开发有限公司 | A kind of vertical methanol tank circulated sprinkling cooling system |
| CN209796376U (en) * | 2019-03-06 | 2019-12-17 | 无锡南泉压力容器有限公司 | Storage tank with spraying device |
| CN212830518U (en) * | 2020-05-08 | 2021-03-30 | 中国成达工程有限公司 | Fire-fighting cooling water diversion facility for storage tank and storage tank |
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