CN201529522U - Device for manufacturing disinfectant - Google Patents
Device for manufacturing disinfectant Download PDFInfo
- Publication number
- CN201529522U CN201529522U CN2009200487483U CN200920048748U CN201529522U CN 201529522 U CN201529522 U CN 201529522U CN 2009200487483 U CN2009200487483 U CN 2009200487483U CN 200920048748 U CN200920048748 U CN 200920048748U CN 201529522 U CN201529522 U CN 201529522U
- Authority
- CN
- China
- Prior art keywords
- vertical tube
- water
- exhaust outlet
- hydrochloric acid
- vertical
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Abstract
A device for manufacturing disinfectant with hypochlorous acid as the main ingredient adopts the structure that the device main body adopts a vertical cylinder with an exhaust port formed at the upper end and a product outlet formed at the lower end, a solvent water (tap water or well water) filling opening is formed on the side surface at the upper end of the vertical cylinder, an air feeding opening is formed on the side surface at the lower end of the vertical cylinder, a sodium hypochlorite solution filling opening and a hydrochloric acid solution filling opening are formed between the lower part of the tap water filling opening and the upper part of the air feeding opening in sequence at certain intervals, so that solvent water, sodium hypochlorite solution and hydrochloric acid solution are completely mixed in sequence from the top down, at the same time, air is continuously pressed in from the air feeding opening on the lower side of the vertical cylinder and gas generated by reaction flows from the bottom up, so that various solutions, solutes and solvents are completely mixed layer by layer, solvent water is cleaned, chlorine gas is reclaimed, odor in the product is removed, and high-quality disinfectant is generated.
Description
Technical field
The utility model relates to a kind of manufacturing installation that contains hypochlorous thimerosal, more particularly be exactly with running water or well water etc. as solvent, attach, mix the device that liquor natrii hypochloritis and hydrochloric acid solution are made the hypochlorous acid thimerosal.
Background technology
With the thimerosal of hypochlorous acid (HClO) as main component, to the typhoid fever bacterium, coliform, staphylococcus, the bactericidal effect of the harmful bacteria of detection of Salmonella etc. is good, and is harmless, widely used by bakery and confectionery and average family.Such thimerosal, adopt running water or well water to generate as the acidic aqueous solution of solvent, mixing clorox (NaClO) and hydrochloric acid (HCl), but, the control of the amount of the acidic aqueous solution that mixes is difficult to, and the acid aspect of pH value deflection will make the reaction of clorox and hydrochloric acid produce harmful gas-chlorine (CI
2).
At present, in order to be suppressed at the generation of making chlorine in the thimerosal process, adopt multiple improved thimerosal to generate method and apparatus, as the water solution flow amount detecting device is set, flow according to the aqueous solution of supply channel, the mixing addition of adjusting aqueous sodium hypochlorite solution and aqueous hydrochloric acid solution is to keep the pH value, control chlorine a small amount of generation or do not take place fully, add when can this mode must avoid the acid aqueous solution of aqueous sodium hypochlorite solution and salt, each aqueous solution is added gradually, make it reaction lentamente, so be not Perfected process.In addition, utilized carbon dioxide that pH value cushioning effect is generated thimerosal method and device in addition.This method is in the container that institute level pressure power carbon dioxide has been filled, hypochloric acid water solution and aqueous hydrochloric acid solution that the aqueous solution has separately been diluted mix while supplying with, carry out the dissolving of carbon dioxide when mixing, be easy to ensure thimerosal concentration and pH.But shortcoming need to be the co 2 liquefaction gas cylinder, and simultaneously, the process of aqueous solution modulation hypochloric acid water solution and aqueous hydrochloric acid solution and the device of twice aqueous solution process constitute complicated.
Summary of the invention
Technical problem to be solved in the utility model is to have overcome the problem that prior art exists, and provides a kind of and can produce highly purified thimerosal by simple structure, can prevent the thimerosal manufacturing installation of chlorine discharging environmental pollution again.
For solving the problems of the technologies described above, the utility model is to adopt following technical scheme to realize: adopt the upper end that exhaust outlet is set, the lower end is provided with the vertical tube of product outlet product pipe, vertically the upper side of tube has the water ascending pipe, vertically vertical tube lower end side is provided with air supply pipe, and the below that flows down the position of this water ascending pipe to air supply pipe top has clorox ascending pipe and hydrochloric acid ascending pipe according to deciding intervening sequences certainly.
Described water ascending pipe is being configured near the inside of vertical tube: laterally inserted water ascending pipe on the body wall of vertical tube, the water ascending pipe has a plurality of downward ozzles in the bottom of a vertical tube inner tip part, be provided with the inner chamber dividing plate that has a plurality of uniform little open-works on periphery sealing, the plate face in the bottom of ozzle vertical tube inner chamber is separated up and down, the central vertical of this inner chamber dividing plate is installed and is communicated with the bending conduit that vertical tube is gone up lower inner cavity.
Have a plurality of uniform little open-works on the described inner chamber dividing plate, little open-work is of a size of the gas that can make cavity of resorption and flows out by stoping top liquid again.
Described bending conduit structure is that the upper end has the cap that prevents that liquid from splashing into, the position that the side exceeds plane certain distance on the inner chamber dividing plate has inflow entrance, the lower end be Rotate 180 ° opening upwards and connect the sweep of the flow export that exceeds bending conduit extreme lower position certain altitude.
Clorox ascending pipe described in the technical scheme the inside of vertical tube near is constructed identical near the structure inside of vertical tube with the water ascending pipe with the hydrochloric acid ascending pipe.
To be the vertical tube described in the first cover technical scheme be divided into independently the first vertical vertical vertical tube of tube and the 3rd of tube, second according near water ascending pipe, clorox ascending pipe and the hydrochloric acid ascending pipe structure inside of vertical tube to the second cover technical scheme of implementing the thimerosal manufacturing installation.
The described first vertical tube is provided with exhaust outlet in the upper end, the lower end is provided with first leakage fluid dram, the upper side of the first vertical tube has the water ascending pipe, lower end side is provided with first air supply pipe, and the water ascending pipe is identical near the water ascending pipe structure vertical inside described near the structure inside of vertical tube and the first cover technical scheme.
Vertically the tube structure is identical with the first vertical tube structure with the 3rd for the described second vertical tube, is connected with woven hose with ventilation duct between 3 tubes.
Utilize the upper end that exhaust outlet is set, the vertical tube of lower end preparation product pipe, from then on vertically the top of tube is poured water (running water or well water) in vertical tube, below the position under the current, vertically in order clorox and hydrochloric acid are being injected at interval with definite in the tube, simultaneously, air supply pipe constantly is pressed into air from vertical tube downside, input gas and reaction generate gas flow upward stir, mixed solution, input recycled in the tube lower end again after gas was derived by exhaust outlet, and lower end preparation product pipe is derived the thimerosal manufacture method.
Water in the inside gas-liquid mixed mode of vertical tube is, water flows into from the water ascending pipe, water is divided into many rills and sprays from top to bottom and enter bubbling area by fine behind ozzle, and retain in the groove that constitutes by bending conduit and inner chamber dividing plate, the water of sprinkling has increased the contact area with intracavity gas.
Compressor is squeezed into compressed air by air supply pipe and is made that gas moves from bottom to top in the tube in vertical tube, the little open-work of gas on the inner chamber dividing plate is absorbed and filters chlorine when upwards flowing through solution, and stop the liquid on the inner chamber dividing plate to flow down, enter air supply pipe by exhaust outlet and circulation air supply pipe then and recycle from little open-work.
Because the inflow entrance and the inner chamber dividing plate of bending conduit have difference in height, water is retained above the inner chamber dividing plate, the water that exceeds inflow entrance can flow in the bending conduit from inflow entrance, flow export and sweep have difference in height, the water that flows in the bending conduit can accumulate in pipe, prevent that gas from passing through thus, enter next bubbling area along with the unnecessary water of the continuous inflow of water can flow out from sweep.Utilize in the bubbling area spray water that the top flows down and from the gas of below spray, gas-liquid convection, solution is fully mixed.
Clorox is identical in the inside gas-liquid mixed mode of vertical tube with water in the inside gas-liquid mixed mode of vertical tube with hydrochloric acid.
Aqueous vapor liquid contact zone gas and liquid do not react, and water will reclaim less than the chlorine flushing of reclaiming; In the clorox bubbling area, the water of inflow mixes with clorox, and absorbs the chlorine that hydrochloric acid reaction taken place and contact reaction again with clorox, becomes the zone of neutralization and recovery chlorine; In water, clorox, the mixed in hydrochloric acid district, clorox, hydrochloric acid fully react, and simultaneously, the chlorine that is dissolved in the liquid are evaporated, and remove the smell of chlorine in the product, and generate high-quality product-thimerosal.
Compared with prior art the beneficial effects of the utility model are:
1. thimerosal manufacturing installation described in the utility model is water pH value stabilization in vertically successively flowing down and clorox, mixed in hydrochloric acid in the tube, can guaranteeing to produce when producing;
2. the gas that thimerosal manufacturing installation reaction described in the utility model produces circulates repeatedly and passes through each layer solution from the bottom to top one by one, fully mix, both absorbed the chlorine of generation, suppress chlorine and discharge the environment ground contamination, can remove the chlorine smell again, improve the quality of commodity;
3. thimerosal manufacturing installation described in the utility model is simple in structure, and attendant equipment is few, and it is simple to produce needed raw material, so can seek the simplification of device and the attenuating of generation price;
4. the vertical tube of thimerosal manufacturing installation described in the utility model can be a unit with the inlet of each point, is divided into 3 independently structural units, and the equipment whole height is reduced, and not limited by factory building height, relaxes setting up production site etc. condition being corresponding.
Description of drawings
Below in conjunction with accompanying drawing the utility model is further described:
Fig. 1 is the concept map of thimerosal manufacturing installation in the utility model;
Fig. 2 is near an in-built part expanded view the water ascending pipe in Fig. 1;
Fig. 3 is to be the concept map of the manufacturing installation after unit is cut apart with individual inlet with vertical cylindrical shell.
Among the figure:
1 vertical tube
1a first is tube vertically
1b second is tube vertically
1c the 3rd is tube vertically
11 exhaust outlets
12 product pipes
13 inner chamber dividing plates
14 bending conduits
15 first leakage fluid drams
16 second ascending pipes
17 second leakage fluid drams
18 the 3rd ascending pipes
21 water ascending pipes
22 clorox ascending pipes
23 hydrochloric acid ascending pipes
31 air supply pipes
32 circulation air supply pipes
34 the 3rd exhaust outlets
35 second air supply pipes
36 second exhaust outlets
37 first air supply pipes
41,42,43 woven hoses
51,52,53 ventilation ducts
131 little open-works
141 caps
142 inflow entrances
143 sweeps
144 flow exports
211 ozzles
A1, A2, A3 bubbling area
The C compressor
P1, P2, P3 pump
The specific embodiment
Below in conjunction with accompanying drawing the utility model is explained in detail:
Consult Fig. 1, Fig. 2, the thimerosal manufacturing installation adopts the upper end that exhaust outlet 11 is set, the lower end is provided with the vertical tube 1 of product outlet product pipe 12, vertically the upper side of tube 1 has water ascending pipe 21, vertically tube 1 lower end side is provided with air supply pipe 31, exhaust outlet 11 inserts air supply pipe 31 by circulation air supply pipe 32, and the below that flows down the position of this water ascending pipe 21 to air supply pipe 31 tops have clorox ascending pipe 22 and hydrochloric acid ascending pipe 23 according to deciding intervening sequences certainly.
Consult Fig. 2, water ascending pipe 21 is being configured near the inside of vertical tube 1: laterally inserted water ascending pipe 21 on the body wall of vertical tube 1, water ascending pipe 21 has a plurality of downward ozzles 211 in the bottom of vertical tube 1 an inner tip part, the bottom of ozzle 211 be provided with have a plurality of uniform little open-works 131 on periphery sealing, the plate face inner chamber dividing plate 13 vertically tube 1 inner chamber separate up and down, little open-work 131 is of a size of the gas that can make cavity of resorption and flows out by stoping top liquid again.The central vertical of this inner chamber dividing plate 13 is installed and is communicated with the bending conduit 14 that vertical tube is gone up lower inner cavity, bending conduit 14 structures are that the upper end has the cap 141 that prevents that liquid from splashing into, the position that the side exceeds plane certain distance on the curtain wall penel has inflow entrance 142, the lower end be Rotate 180 ° opening upwards and connect the sweep 143 of the flow export 144 that exceeds bending conduit extreme lower position certain altitude.Clorox ascending pipe 22 the inside of vertical tube 1 near is constructed identical near the structure inside of vertical tube 1 with water ascending pipe 21 with hydrochloric acid ascending pipe 23.
Consult Fig. 2, Fig. 3, the second cover technical scheme of implementing the thimerosal manufacturing installation is that the vertical tube 1 described in the first cover technical scheme is divided into independently first vertical 1a, second vertical 1b and the 3rd vertical 1c according near water ascending pipe 21, clorox ascending pipe 22 and the hydrochloric acid ascending pipe 23 structure inside of vertical tube 1.Water ascending pipe 21, clorox ascending pipe 22 and hydrochloric acid ascending pipe 23 are identical near the structure vertical 1 inside described near the structure inside of vertical tube 1 and the first cover technical scheme.The second cover technical scheme and the first cover technical scheme difference are that the first vertical tube is provided with exhaust outlet 11 in the upper end, and the upper side that the lower end is provided with first leakage fluid dram, 15, the first vertical tubes has water ascending pipe 21, and lower end side is provided with first air supply pipe 37.The second vertical tube is provided with second exhaust outlet 36 in the upper end, the upper side that the lower end is provided with second leakage fluid dram, 17, the second vertical tubes has second ascending pipe 16, and lower end side is provided with second air supply pipe 35.The 3rd vertical tube is provided with the 3rd exhaust outlet 34 in the upper end, the upper side that the lower end is provided with product pipe 12, the three vertical tubes has the 3rd ascending pipe 18, and lower end side is provided with air supply pipe 31.
Consult Fig. 3, first leakage fluid dram 15 inserts pump P1 with clorox ascending pipe 22, pump P1 is connected with second ascending pipe 16 by woven hose 41, second leakage fluid dram 17 inserts pump P2 with hydrochloric acid ascending pipe 23, pump P2 is connected with the 3rd ascending pipe 18 by woven hose 42, and product pipe 12 is exported finished product by pump P3 and woven hose 43.Compressor C connects ventilation duct 53, and exhaust outlet 11 and ventilation duct 53 insert air supply pipe 31, the three exhaust outlets 34 and insert second air supply pipe, 35, the second exhaust outlets 36 by ventilation duct 51 accesses first air supply pipe 37 by ventilation duct 52.
Consult Fig. 1, Fig. 2, the utility model from top to bottom fully mixes each raw material liq by inserting water ascending pipe 21, clorox ascending pipe 22 and hydrochloric acid ascending pipe 23 from top to bottom successively in vertical tube 1 side successively, simultaneously, air supply pipe 31 constantly is pressed into air from vertical tube 1 downside, and the gas that reaction is produced is from bottom to top successively by various solution.Each solution hybrid mode is, at first, water enters bubbling area A1, the chlorine that reaction here generates is by the water-soluble part of separating, reduce the chlorine content in the emission gases, then, liquid among the bubbling area A1 enters bubbling area A2 with the liquor natrii hypochloritis who comes in by clorox ascending pipe 22 to be mixed, the chlorine that has taken place for hydrochloric acid reaction is absorbed a part and contacts with clorox and react in bubbling area A2, become neutralization and the zone of reclaiming chlorine, then, liquid among the bubbling area A2 enters bubbling area A3 with the hydrochloric acid solution of coming in by hydrochloric acid ascending pipe 23 to be mixed, chlorine is cleaned smell, become the zone that chlorine flavor in the thimerosal removes and generate effect product sterilization liquid, effect product sterilization liquid is derived by lower end product pipe 12, and the chlorine that produces in the reaction is blown into to participate in the vertical tube 1 by air supply pipe 31 again through circulation air supply pipe 32 by exhaust outlet 11 discharges and reacts.
Consult Fig. 2, water ascending pipe 21 is structure part expanded view near the inside of vertical tube 1, water shown in the figure flows into from water ascending pipe 21, water is divided into many rills and sprays from top to bottom and enter bubbling area A1 by fine behind ozzle 211, and retain in the groove that constitutes by bending conduit 14 and inner chamber dividing plate 13, the water of sprinkling has increased the contact area with intracavity gas.
Consult Fig. 1, Fig. 2, compressor C squeezes into compressed air by air supply pipe 31 and makes that gas moves from bottom to top in the tube in vertical tube 1, the little open-work 131 of gas on inner chamber dividing plate 13 is absorbed and filters chlorine when upwards flowing through solution, and stop the liquid on the inner chamber dividing plate 13 to flow down, enter air supply pipe 31 by exhaust outlet 11 and circulation air supply pipe 32 then and recycle from little open-work 131.
Because the inflow entrance 142 and the inner chamber dividing plate 13 of bending conduit 14 have difference in height, water is retained above inner chamber dividing plate 13, the water that exceeds inflow entrance 142 can flow in the bending conduit 14 from inflow entrance 142, flow export 144 has difference in height with sweep 143, the water that flows in the bending conduit 14 can accumulate in pipe, prevent that gas from passing through thus, enter bubbling area A2 along with the unnecessary water of the continuous inflow of water can flow out from sweep 143.
Bubbling area A2 and bubbling area A3 structure is identical with bubbling area A1 structure, all utilizes spray water that the top flows down and from gas injection, the gas-liquid convection of below, solution is fully mixed.No matter the first cover technical scheme and second is overlapped technical scheme, and gas and liquid do not react in bubbling area A1, and water will reclaim less than the chlorine flushing of reclaiming; The water that is flowed into by bubbling area A1 mixes with the clorox that is entered by clorox ascending pipe 22 in bubbling area A2, absorbs chlorine that hydrochloric acid reaction taken place and contact with clorox and react, and becomes to neutralize and the zone of recovery chlorine; Mixed solution enters bubbling area A3 to be mixed with the hydrochloric acid that is entered by hydrochloric acid ascending pipe 23 again, and fully reaction makes the chlorine that is dissolved in the liquid evaporate simultaneously, removes the smell of chlorine in the product, and generates high-quality effect product sterilization liquid.
Claims (3)
1. the manufacturing installation of a thimerosal, it is characterized in that this device is a main body by the vertical tube that exhaust outlet is set in the upper end, is provided with products export in the lower end, from this vertically tube exhaust outlet to the product pipe according to certain interval punching, the water inlet is set from top to bottom in order, liquor natrii hypochloritis's inlet, the hydrochloric acid solution inlet, air supply opening.
2. thimerosal manufacturing installation is characterized in that this device is provided with three the vertical tube that exhaust outlet, lower end be provided with leakage fluid dram by the upper end and constitutes; The first vertical tube is provided with exhaust outlet in the upper end, and the lower end is provided with leakage fluid dram, and this leakage fluid dram is provided with the clorox inlet with the centre of the woven hose that the second vertical tube upper end is connected; The exhaust outlet of the second vertical tube links to each other by snorkel with first vertical tube lower end side; Second vertical middle inlet that is provided with hydrochloric acid solution of woven hose that leakage fluid dram is connected with the 3rd vertical tube upper end; The exhaust outlet of the 3rd vertical tube is connected by snorkel with second vertical tube lower end side; Adopt pressing mode to the 3rd vertical lower end side air supply opening supply gas, the liquid outlet of the 3rd vertical tube is products export.
3. according to the described thimerosal manufacturing installation of claim 2, it is characterized in that the exhaust outlet of the described first vertical tube is connected with the air supply opening of the 3rd vertical tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200487483U CN201529522U (en) | 2009-10-28 | 2009-10-28 | Device for manufacturing disinfectant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200487483U CN201529522U (en) | 2009-10-28 | 2009-10-28 | Device for manufacturing disinfectant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201529522U true CN201529522U (en) | 2010-07-21 |
Family
ID=42524933
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009200487483U Expired - Fee Related CN201529522U (en) | 2009-10-28 | 2009-10-28 | Device for manufacturing disinfectant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201529522U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110523319A (en) * | 2019-08-27 | 2019-12-03 | 广州泰道安医疗科技有限公司 | A kind of disinfectant production technology |
| CN111232929A (en) * | 2020-03-24 | 2020-06-05 | 乔卫峰 | Equipment for preparing hypochlorous acid solution and hypochlorous acid solution preparation process |
| CN115443973A (en) * | 2022-09-30 | 2022-12-09 | 黑龙江省农业科学院植物保护研究所 | Corn borer pest prevention and control equipment |
-
2009
- 2009-10-28 CN CN2009200487483U patent/CN201529522U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110523319A (en) * | 2019-08-27 | 2019-12-03 | 广州泰道安医疗科技有限公司 | A kind of disinfectant production technology |
| CN110523319B (en) * | 2019-08-27 | 2021-12-10 | 广州泰道安医疗科技有限公司 | Disinfectant fluid production process |
| CN111232929A (en) * | 2020-03-24 | 2020-06-05 | 乔卫峰 | Equipment for preparing hypochlorous acid solution and hypochlorous acid solution preparation process |
| CN115443973A (en) * | 2022-09-30 | 2022-12-09 | 黑龙江省农业科学院植物保护研究所 | Corn borer pest prevention and control equipment |
| CN115443973B (en) * | 2022-09-30 | 2023-09-19 | 黑龙江省农业科学院植物保护研究所 | Corn borer pest control equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201529522U (en) | Device for manufacturing disinfectant | |
| CN104174260B (en) | A kind of absorption column of gas and using method thereof | |
| CN105603452A (en) | Novel efficient sodium hypochlorite generator | |
| CN202400987U (en) | Cleaning system of acetylene gas | |
| CN202226657U (en) | Production system for preparing hydrochloric acid by absorbing hydrogen chloride | |
| CN110898620A (en) | Fountain exhaust gas purification device | |
| CN201437505U (en) | Inclined plate chlorine dioxide reactor | |
| CN206799748U (en) | A kind of electrolytic sodium chloride solution containment | |
| CN205133188U (en) | Ammonia nitrogen blows and takes off device | |
| CN204996321U (en) | Kiln exhaust treatment device | |
| CN217511825U (en) | Novel sodium hypochlorite generation device | |
| CN101575105B (en) | Equipment for preparing medical natrium bicarbonicum | |
| CN107902627A (en) | A kind of high purity chlorine dioxide generator | |
| CN214009201U (en) | A boiler heating power oxygen-eliminating device for polymer monomer production | |
| CN205204957U (en) | Utilize carbide slag to handle device that contains industry hydrochloric acid waste water | |
| CN203021296U (en) | Chlorine dioxide gas generator | |
| CN206762604U (en) | Alkaline dry chlorine equipment | |
| CN111362343A (en) | Method and equipment for extracting bromine from seawater by air blowing method | |
| CN105084317B (en) | A kind of sterilizing machine that Chlorine Dioxide Gas is prepared in situ | |
| CN204778840U (en) | Polyphosphoric acid substep formula synthesis device | |
| CN207605570U (en) | A kind of ClO 2 solution, which is produced, uses absorption tower | |
| CN205954119U (en) | A sodium chlorate reactor for synthetic method chlorine dioxide prepares system | |
| CN204017638U (en) | A kind of absorption column of gas | |
| CN206762605U (en) | Efficient alkaline chlorine gas drying tower | |
| CN204237556U (en) | The vacuum forming apparatus of chlorine dioxide preparation system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100721 Termination date: 20121028 |