CN208493758U - A kind of glass steel tower - Google Patents

A kind of glass steel tower Download PDF

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Publication number
CN208493758U
CN208493758U CN201821037335.0U CN201821037335U CN208493758U CN 208493758 U CN208493758 U CN 208493758U CN 201821037335 U CN201821037335 U CN 201821037335U CN 208493758 U CN208493758 U CN 208493758U
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Prior art keywords
sulfuric acid
tower body
collecting tank
tower
inlet
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CN201821037335.0U
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熊相荣
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CHENGDU MUSHAN FRP Co Ltd
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CHENGDU MUSHAN FRP Co Ltd
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Abstract

The utility model relates to glass fiber reinforced plastics product technical fields, disclose a kind of glass steel tower, including tower body, tower body upper end is provided with gas outlet, tower body side is provided with air inlet, air jet pipe is provided in tower body, air jet pipe is connected to air inlet, the top of air jet pipe is disposed with multiple groups bubble cap tray from bottom to up, collecting tank is provided with below air jet pipe, condenser pipe is provided in collecting tank, extend tower body and connected with water circulating apparatus in the both ends of condenser pipe, the other side of tower body is provided with inlet, the side of tower collecting tank is provided with liquid outlet, sulfuric acid circulation mechanism is provided between liquid outlet and inlet, the top of inlet and be located at tower body be internally provided with packing layer.The utility model installs condenser pipe by the way that collecting tank is arranged in drying tower body in collecting tank, and the concentrated sulfuric acid after water suction can cool in collecting tank, solves the problems, such as the existing drying tower excessively high influence drying efficiency of concentrated sulfuric acid temperature at work.

Description

A kind of glass steel tower
Technical field
The utility model relates to glass reinforced plastic equipment technical field, in particular to a kind of glass steel towers.
Background technique
Glass reinforced plastic (FRP) is also referred to as GFRP, i.e. fiber-reinforced plastic, refer generally to glass fiber reinforcement unsaturated polyester, Epoxy resin and phenolic resin as matrix resin have many advantages, such as that corrosion-resistant, high-strength light, hot property are good, processing performance is excellent, can be wide It is general to be used for glass reinforced plastic preparing chlorine gas drying tower.
Chlorine treatment is the critical process in chlor-alkali production, and task is that the moist chlorine come to electrolysis carries out cooling, drying And pressurized delivered.If the chlorine water content after persulfuric acid is dry is exceeded, the pipe of the processes such as chlorine gas transfer and liquid chlorine will be aggravated Road and equipment corrosion, have serious consequences to entire production system.Industrially use desiccant of the concentrated sulfuric acid as chlorine, be by Chemical reaction occurs in concentrated sulfuric acid dehydration efficiency with higher, not with chlorine, the advantages such as solubility of the chlorine in sulfuric acid is low.
It is reduced since the concentrated sulfuric acid can generate heat and concentration after absorbing moisture, drying of the concentrated sulfuric acid to chlorine at this time Effect is excessively poor, then how to cool down the concentrated sulfuric acid without stopping work and the concentrated sulfuric acid is made to keep a certain concentration cyclic drying chlorine Gas becomes those skilled in the art's technical issues that need to address.
Utility model content
Based on problem above, the utility model provides a kind of glass steel tower.The utility model can realize the feelings that do not stop work The purpose of the cooling concentrated sulfuric acid, by the way that collecting tank is arranged in drying tower body, and installs condenser pipe, after water suction in collecting tank under condition The concentrated sulfuric acid can cool in collecting tank, solve the excessively high influence drying of concentrated sulfuric acid temperature at work of existing drying tower The problem of efficiency.
In order to solve the above technical problems, the technical solution adopted in the utility model is as follows:
A kind of glass steel tower, including tower body, tower body upper end are provided with gas outlet, and tower body side is provided with air inlet, tower body It is inside provided with air jet pipe, air jet pipe is connected to air inlet, and the top of air jet pipe is disposed with multiple groups bubble cap tray from bottom to up, spray It is provided with collecting tank below tracheae, condenser pipe is provided in collecting tank, tower body is extended at the both ends of condenser pipe and water circulation is set Standby connection, the other side of tower body are provided with inlet, and the side of tower collecting tank is provided with liquid outlet, between liquid outlet and inlet It is provided with sulfuric acid circulation mechanism, the top of the inlet and is located at tower body and is internally provided with packing layer.
In the present invention, moist chlorine after cooling enters air jet pipe through the air inlet of tower body side, passes through air jet pipe Nozzle spray into tower body inside, because gas and liquid are influenced difference by self gravity, partial moisture is downwardly into collecting tank In, in the process the concentrated sulfuric acid by sulfuric acid circulation mechanism be transported to below tower body tower body top and by inlet into Enter inside tower body, sprayed out from top to bottom into the concentrated sulfuric acid inside tower body and is connect with the multiple groups bubble cap tray being mounted on inside tower body Touching forms sulfuric acid foam, and moist chlorine persistently rises at this time contacts with the multiple groups bubble cap tray being arranged in above air jet pipe, passes through bubble-cap The concentrated sulfuric acid foam that is formed on plate and remove moisture, the concentrated sulfuric acid after partially contacting with moist chlorine passes through multiple groups bubble cap tray and enters collection In liquid pool, the concentrated sulfuric acid after absorbing moisture at this time has amount of heat, by the condenser pipe that is arranged in collecting tank to the concentrated sulfuric acid It is cooled down.The utility model can be realized do not stop work in the case where the cooling concentrated sulfuric acid purpose, by being arranged in drying tower body Collecting tank, and condenser pipe is installed in collecting tank, the concentrated sulfuric acid after water suction can cool in collecting tank, solve existing Drying tower at work concentrated sulfuric acid temperature excessively high influence drying efficiency the problem of.
As a preferred mode, sulfuric acid circulation mechanism includes sulfuric acid tank, and the side of sulfuric acid tank is provided with sulfuric acid pump one, Sulfuric acid pump one is connected to liquid outlet, and the other side of sulfuric acid tank is provided with sulfuric acid pump two, is vertically arranged with connecting tube on sulfuric acid pump two One, the side of connecting tube one is provided with head tank, and the lower end of head tank is provided with connecting tube two, and connecting tube two runs through the side of tower body Wall is simultaneously provided with nozzle.
As a preferred mode, PH detector is additionally provided on the outside of collecting tank, the test side of PH detector is run through The one side wall of collecting tank.
As a preferred mode, bubble cap tray is set as four groups and is horizontally arranged inside tower body.
As a preferred mode, the other side of collecting tank is additionally provided with concentrated sulfuric acid import.
As a preferred mode, packing layer includes packing support plate, and packing support plate upper surface is provided with Pall ring Filler, Pall ring filler upper end are provided with fixed network board.
As a preferred mode, the mistake of the mineral wool production using dipping fluorine containing silicone oil is provided with above packing layer Strainer, the tower body are made of glass reinforced plastic.
Compared with prior art, the utility model has the beneficial effects that
(1) the utility model can be realized do not stop work in the case where the cooling concentrated sulfuric acid purpose, by being set in drying tower body Collecting tank is set, and condenser pipe is installed in collecting tank, the concentrated sulfuric acid after water suction can cool in collecting tank, solve existing Drying tower at work concentrated sulfuric acid temperature excessively high influence drying efficiency the problem of.
(2) sulfuric acid circulation mechanism includes sulfuric acid tank in the utility model, and the side of sulfuric acid tank is provided with sulfuric acid pump one, sulfuric acid Pump one is connected to liquid outlet, and the other side of sulfuric acid tank is provided with sulfuric acid pump two, and connecting tube one is vertically arranged on sulfuric acid pump two, even The side of adapter tube one is provided with head tank, and the lower end of head tank is provided with connecting tube two, and connecting tube two runs through the side wall of tower body simultaneously It is provided with nozzle.Sulfuric acid pump one is closed when initialization, and the concentrated sulfuric acid is injected into sulfuric acid tank and opens sulfuric acid pump two, in sulfuric acid pump two Under the action of the concentrated sulfuric acid is inputted in head tank by connecting tube one, the concentrated sulfuric acid in head tank passes through connecting tube two into tower again Internal portion simultaneously sprays out the dehumidifying for carrying out moist chlorine, starts sulfuric acid pump one after the sulfuric acid in collecting tank reaches a certain amount of for liquid collecting The circulation of sulfuric acid is carried out in sulfuric acid input sulfuric acid tank in pond, the sulfuric acid circulation mechanism structure is simple, by head tank convenient for dense Sulfuric acid enters inside tower body and spraying effect is more preferable.
(3) PH detector is additionally provided in the utility model on the outside of collecting tank, liquid collecting is run through in the test side of PH detector The one side wall in pond can check the concentration of sulfuric acid in collecting tank, timely by PH detector convenient for being adjusted according to the actual situation It is whole, guarantee the effect of moist chlorine dehumidifying.
(4) bubble cap tray is set as four groups and is horizontally arranged inside tower body in the utility model, and bubble cap tray is set as four groups, Effect on moisture extraction is good, and space hold is small, can reach the quality requirement of product, and the horizontally disposed increase of bubble cap tray is direct with moist chlorine The area of contact improves dehumidification efficiency.
(5) other side of collecting tank is additionally provided with concentrated sulfuric acid import in the utility model, when the sulfuric acid concentration in collecting tank When not up to standard, high-concentration sulfuric acid can be injected by concentrated sulfuric acid import, to improve the concentration of the concentrated sulfuric acid in collecting tank, and be followed with sulfuric acid Ring mechanism cooperation achievees the purpose that sulfuric acid is recycled in a certain concentration.
(6) packing layer includes packing support plate in the utility model, and packing support plate upper surface is provided with Pall ring filler, Pall ring filler upper end is provided with fixed network board, and packing support plate plays a supportive role to filler, carries packing support plate and fixed net The stability in filler use process is improved under plate collective effect, Pall ring filler, which obtains, to be easy, and using effect is good.
(7) filtering of the mineral wool production using dipping fluorine containing silicone oil is provided in the utility model above packing layer Net, the tower body are made of glass reinforced plastic, and moist chlorine can have part acid mist after the concentrated sulfuric acid dehumidifies, and pass through dipping fluorine containing silicone oil The filter screen of mineral wool production can remove acid mist, and the chlorine after making drying reaches product requirement, and has corrosion-resistant, light The advantages that matter is high-strength, hot property is good, processing performance is excellent.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Wherein, the gas outlet 1-, 2- filter screen, 3- packing layer, 3-1- fixed network board, 3-2- filler, 3-3- packing support plate, 4- nozzle, 5- connecting tube two, 6- tower body, 7- bubble cap tray, 8- air jet pipe, 9- air inlet, the import of the 10- concentrated sulfuric acid, 11-PH detection Instrument, 12- head tank, 13- connecting tube one, 14- sulfuric acid pump two, 15- sulfuric acid tank, 16- sulfuric acid pump one, 17- collecting tank, 18- condensation Pipe.
Specific embodiment
The utility model will be further described below with reference to the accompanying drawings.The embodiments of the present invention includes but unlimited In the following example.
Embodiment 1:
Referring to Fig. 1, a kind of glass steel tower, including tower body 6,6 upper end of tower body are provided with gas outlet 1, and 6 side of tower body is provided with Air inlet 9, it is characterised in that: air jet pipe 8 is provided in the tower body 6, air jet pipe 8 is connected to air inlet 9, air jet pipe 8 it is upper Side is disposed with multiple groups bubble cap tray 7 from bottom to up, and the lower section of air jet pipe 8 is provided with collecting tank 17, is provided in collecting tank 17 Condenser pipe 18, the both ends of condenser pipe 18 are extended tower body 6 and are connected with water circulating apparatus, and water circulating pump can be selected in water circulating apparatus, The other side of tower body 6 is provided with inlet, and the side of tower collecting tank 17 is provided with liquid outlet, is arranged between liquid outlet and inlet There is a sulfuric acid circulation mechanism, the top of the inlet and is located at tower body 6 and is internally provided with packing layer 3.
In the present invention, moist chlorine after cooling enters air jet pipe through the air inlet of tower body side, passes through air jet pipe Nozzle spray into tower body inside, because gas and liquid are influenced difference by self gravity, partial moisture is downwardly into collecting tank In, in the process the concentrated sulfuric acid by sulfuric acid circulation mechanism be transported to below tower body tower body top and by inlet into Enter inside tower body, sprayed out from top to bottom into the concentrated sulfuric acid inside tower body and is connect with the multiple groups bubble cap tray being mounted on inside tower body Touching forms sulfuric acid foam, and moist chlorine persistently rises at this time contacts with the multiple groups bubble cap tray being arranged in above air jet pipe, passes through bubble-cap The concentrated sulfuric acid foam that is formed on plate and remove moisture, the concentrated sulfuric acid after partially contacting with moist chlorine passes through multiple groups bubble cap tray and enters collection In liquid pool, the concentrated sulfuric acid after absorbing moisture at this time has amount of heat, by the condenser pipe that is arranged in collecting tank to the concentrated sulfuric acid It is cooled down.The utility model can be realized do not stop work in the case where the cooling concentrated sulfuric acid purpose, by being arranged in drying tower body Collecting tank, and condenser pipe is installed in collecting tank, the concentrated sulfuric acid after water suction can cool in collecting tank, solve existing Drying tower at work concentrated sulfuric acid temperature excessively high influence drying efficiency the problem of.
Embodiment 2:
Referring to Fig. 1, a kind of glass steel tower, including tower body 6,6 upper end of tower body are provided with gas outlet 1, and 6 side of tower body is provided with Air inlet 9, it is characterised in that: air jet pipe 8 is provided in the tower body 6, air jet pipe 8 is connected to air inlet 9, air jet pipe 8 it is upper Side is disposed with multiple groups bubble cap tray 7 from bottom to up, and the lower section of air jet pipe 8 is provided with collecting tank 17, is provided in collecting tank 17 Condenser pipe 18, the both ends of condenser pipe 18 are extended tower body 6 and are connected with water circulating apparatus, and water circulating pump can be selected in water circulating apparatus, The other side of tower body 6 is provided with inlet, and the side of tower collecting tank 17 is provided with liquid outlet, is arranged between liquid outlet and inlet There is a sulfuric acid circulation mechanism, the top of the inlet and is located at tower body 6 and is internally provided with packing layer 3.
Sulfuric acid circulation mechanism includes sulfuric acid tank 15, and the side of sulfuric acid tank 15 is provided with sulfuric acid pump 1, one 16 He of sulfuric acid pump Liquid outlet connection, the other side of sulfuric acid tank 15 are provided with sulfuric acid pump 2 14, connecting tube 1 are vertically arranged on sulfuric acid pump 2 14, The side of connecting tube 1 is provided with head tank 12, and the lower end of head tank 12 is provided with connecting tube 25, and connecting tube 25 runs through tower The side wall of body 6 is simultaneously provided with nozzle 4.
In the present embodiment, sulfuric acid pump one is closed when initialization, and the concentrated sulfuric acid is injected into sulfuric acid tank and opens sulfuric acid pump two, The concentrated sulfuric acid is inputted in head tank by connecting tube one under the action of sulfuric acid pump two, the concentrated sulfuric acid in head tank passes through connecting tube again Two enter inside tower body and spray out the dehumidifying for carrying out moist chlorine, start sulfuric acid pump after the sulfuric acid in collecting tank reaches a certain amount of One will carry out the circulation of sulfuric acid in the sulfuric acid input sulfuric acid tank in collecting tank, the sulfuric acid circulation mechanism structure is simple, passes through a high position Slot enters inside tower body convenient for the concentrated sulfuric acid and spraying effect is more preferable.
The other side of collecting tank 17 is additionally provided with concentrated sulfuric acid import 10.In which, when the sulfuric acid concentration in collecting tank not When up to standard, high-concentration sulfuric acid can be injected by concentrated sulfuric acid import, to improve the concentration of the concentrated sulfuric acid in collecting tank, and be recycled with sulfuric acid Mechanism cooperation achievees the purpose that sulfuric acid is recycled in a certain concentration.
The other parts of the present embodiment are same as Example 1, just repeat no more here.
Embodiment 3:
Referring to Fig. 1, a kind of glass steel tower, including tower body 6,6 upper end of tower body are provided with gas outlet 1, and 6 side of tower body is provided with Air inlet 9, it is characterised in that: air jet pipe 8 is provided in the tower body 6, air jet pipe 8 is connected to air inlet 9, air jet pipe 8 it is upper Side is disposed with multiple groups bubble cap tray 7 from bottom to up, and the lower section of air jet pipe 8 is provided with collecting tank 17, is provided in collecting tank 17 Condenser pipe 18, the both ends of condenser pipe 18 are extended tower body 6 and are connected with water circulating apparatus, and water circulating pump can be selected in water circulating apparatus, The other side of tower body 6 is provided with inlet, and the side of tower collecting tank 17 is provided with liquid outlet, is arranged between liquid outlet and inlet There is a sulfuric acid circulation mechanism, the top of the inlet and is located at tower body 6 and is internally provided with packing layer 3.
The outside of collecting tank 17 is additionally provided with PH detector 11, and the side of collecting tank 17 is run through in the test side of PH detector 11 Wall.
In the present embodiment, the one side wall of collecting tank is run through in the test side of PH detector, can timely be looked by PH detector It sees the concentration of sulfuric acid in collecting tank, convenient for being adjusted according to the actual situation, guarantees the effect of moist chlorine dehumidifying.
As a preferred mode, bubble cap tray 7 is set as four groups and is horizontally arranged inside tower body 6.In which, bubble Cover plate is set as four groups, and effect on moisture extraction is good, and space hold is small, can reach the quality requirement of product, and bubble cap tray is horizontally disposed Increase the area directly contacted with moist chlorine, improves dehumidification efficiency.
The other parts of the present embodiment are same as Example 1, just repeat no more here.
Embodiment 4:
Referring to Fig. 1, a kind of glass steel tower, including tower body 6,6 upper end of tower body are provided with gas outlet 1, and 6 side of tower body is provided with Air inlet 9, it is characterised in that: air jet pipe 8 is provided in the tower body 6, air jet pipe 8 is connected to air inlet 9, air jet pipe 8 it is upper Side is disposed with multiple groups bubble cap tray 7 from bottom to up, and the lower section of air jet pipe 8 is provided with collecting tank 17, is provided in collecting tank 17 Condenser pipe 18, the both ends of condenser pipe 18 are extended tower body 6 and are connected with water circulating apparatus, and water circulating pump can be selected in water circulating apparatus, The other side of tower body 6 is provided with inlet, and the side of tower collecting tank 17 is provided with liquid outlet, is arranged between liquid outlet and inlet There is a sulfuric acid circulation mechanism, the top of the inlet and is located at tower body 6 and is internally provided with packing layer 3.
Packing layer 3 includes packing support plate 3-3, and the upper surface packing support plate 3-3 is provided with Pall ring filler 3-2, Bauer The upper end ring filler 3-2 is provided with fixed network board 3-1.
In the present embodiment, packing support plate plays a supportive role to filler, carries packing support plate and fixed network board collective effect The lower stability improved in filler use process, Pall ring filler, which obtains, to be easy, and using effect is good.
As a preferred mode, the top of packing layer 3 is provided with using the mineral wool production for impregnating fluorine containing silicone oil Filter screen 2, the tower body 6 are made of glass reinforced plastic.In which, moist chlorine can have part acid mist after the concentrated sulfuric acid dehumidifies, and lead to The filter screen for crossing the mineral wool production of dipping fluorine containing silicone oil can remove acid mist, and the chlorine after making drying, which reaches product use, to be wanted It asks, and glass reinforced plastic has many advantages, such as that corrosion-resistant, high-strength light, hot property are good, processing performance is excellent.
The other parts of the present embodiment are same as Example 1, just repeat no more here.
It as above is the embodiments of the present invention.Design parameter in above-described embodiment and embodiment is merely to clear The verification process of the utility model is stated by Chu, not to limit the scope of patent protection of the utility model, the utility model Scope of patent protection is still subject to the claims, made by all specifications and accompanying drawing content with the utility model Equivalent structure variation, similarly should be included in the protection scope of the utility model.

Claims (7)

1. a kind of glass steel tower, including tower body (6), tower body (6) upper end is provided with gas outlet (1), tower body (6) side be provided with into Port (9), it is characterised in that: be provided with air jet pipe (8) in the tower body (6), air jet pipe (8) is connected to air inlet (9), jet The top of pipe (8) is disposed with multiple groups bubble cap tray (7) from bottom to up, is provided with below air jet pipe (8) collecting tank (17), is collected It is provided with condenser pipe (18) in liquid pool (17), the both ends of condenser pipe (18) are extended tower body (6) and are connected to water circulating apparatus, tower body (6) the other side is provided with inlet, and the side of tower collecting tank (17) is provided with liquid outlet, is arranged between liquid outlet and inlet There is a sulfuric acid circulation mechanism, the top of the inlet and is located at tower body (6) and is internally provided with packing layer (3).
2. glass steel tower according to claim 1, it is characterised in that: the sulfuric acid circulation mechanism includes sulfuric acid tank (15), The side of sulfuric acid tank (15) is provided with sulfuric acid pump one (16), and sulfuric acid pump one (16) is connected to liquid outlet, sulfuric acid tank (15) it is another Side is provided with sulfuric acid pump two (14), and connecting tube one (13), the side of connecting tube one (13) are vertically arranged on sulfuric acid pump two (14) It is provided with head tank (12), the lower end of head tank (12) is provided with connecting tube two (5), and connecting tube two (5) runs through the side of tower body (6) Wall is simultaneously provided with nozzle (4).
3. glass steel tower according to claim 2, it is characterised in that: the other side of the collecting tank (17) is additionally provided with dense Sulfuric acid import (10).
4. glass steel tower according to claim 1, it is characterised in that: be additionally provided with PH inspection on the outside of the collecting tank (17) It surveys instrument (11), the one side wall of collecting tank (17) is run through in the test side of PH detector (11).
5. glass steel tower according to claim 4, it is characterised in that: the bubble cap tray (7) is set as four groups and horizontal peace It is internal mounted in tower body (6).
6. glass steel tower according to claim 1, it is characterised in that: described filler layer (3) includes packing support plate (3- 3), the upper surface packing support plate (3-3) is provided with Pall ring filler (3-2), and the upper end Pall ring filler (3-2) is provided with fixed net Plate (3-1).
7. glass steel tower according to claim 6, it is characterised in that: be provided with above described filler layer (3) using leaching The filter screen (2) of the mineral wool production of stain fluorine containing silicone oil, the tower body (6) are made of glass reinforced plastic.
CN201821037335.0U 2018-07-02 2018-07-02 A kind of glass steel tower Active CN208493758U (en)

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CN201821037335.0U CN208493758U (en) 2018-07-02 2018-07-02 A kind of glass steel tower

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Application Number Priority Date Filing Date Title
CN201821037335.0U CN208493758U (en) 2018-07-02 2018-07-02 A kind of glass steel tower

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113398719A (en) * 2021-06-15 2021-09-17 山东东岳氟硅材料有限公司 Device and method for recovering chlorine in tail chlorine
CN114797443A (en) * 2022-03-30 2022-07-29 重庆蓝洁广顺净水材料有限公司 Desulfurization and denitrification device based on biological bacteria

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113398719A (en) * 2021-06-15 2021-09-17 山东东岳氟硅材料有限公司 Device and method for recovering chlorine in tail chlorine
CN114797443A (en) * 2022-03-30 2022-07-29 重庆蓝洁广顺净水材料有限公司 Desulfurization and denitrification device based on biological bacteria

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