CN212467147U - Hydrochloric acid production process enrichment facility - Google Patents
Hydrochloric acid production process enrichment facility Download PDFInfo
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- CN212467147U CN212467147U CN202020301873.7U CN202020301873U CN212467147U CN 212467147 U CN212467147 U CN 212467147U CN 202020301873 U CN202020301873 U CN 202020301873U CN 212467147 U CN212467147 U CN 212467147U
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- hydrochloric acid
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Abstract
The utility model provides a hydrochloric acid production process enrichment facility. The hydrochloric acid production process concentration device comprises a support plate; the evaporation tank is arranged on the supporting plate, and the top and the bottom of the evaporation tank extend out of the supporting plate; the cooling tank is fixedly arranged on one side of the supporting plate; the concentration coil is arranged in the cooling tank, and the air inlet end and the air outlet end of the concentration coil extend out of the cooling tank; first exhaust pipe, first exhaust pipe fixed mounting be in the evaporating pot is close to one side of cooling tank, first exhaust pipe is located the top of evaporating pot, first exhaust pipe give vent to anger the end with cooling coil's inlet end is pegged graft mutually. The utility model provides a hydrochloric acid production process enrichment facility has that concentrated effectual, cooling are stable, and can carry out the advantage of recycling to the cooling water.
Description
Technical Field
The utility model relates to a concentrated technical field of hydrochloric acid especially relates to a hydrochloric acid production process enrichment facility.
Background
Hydrochloric acid is widely used in a plurality of steel production enterprises to clean steel, and concentrated hydrochloric acid can well erode the rust layer on the surface of the steel, thereby facilitating subsequent processing.
However, the existing concentration device has low concentration efficiency and small production yield, and needs a large amount of flowing water for cooling during concentration, so that the existing concentration device is directly discharged after being used for one time and is relatively wasted.
Therefore, there is a need to provide a new concentration device for hydrochloric acid production process to solve the above technical problems.
SUMMERY OF THE UTILITY MODEL
The technical problem solved by the utility model is to provide a concentrated effectual, the cooling is stable, and can carry out the hydrochloric acid production process enrichment facility of recycling to the cooling water.
In order to solve the technical problem, the utility model provides a hydrochloric acid production process enrichment facility includes: a support plate; the evaporation tank is arranged on the supporting plate, and the top and the bottom of the evaporation tank extend out of the supporting plate; the cooling tank is fixedly arranged on one side of the supporting plate; the concentration coil is arranged in the cooling tank, and the air inlet end and the air outlet end of the concentration coil extend out of the cooling tank; the first exhaust pipe is fixedly installed on one side, close to the cooling tank, of the evaporation tank, the first exhaust pipe is located above the evaporation tank, and the air outlet end of the first exhaust pipe is connected with the air inlet end of the concentration coil pipe in an inserted mode; a collection tank disposed below the cooling tank; the drip pipe is arranged on the collecting tank, the top end of the drip pipe extends out of the drip pipe, and the air inlet end of the drip pipe is spliced with the air outlet end of the concentration coil pipe; the waste gas treatment tank is arranged on one side of the collecting tank, which is far away from the evaporation tank; the second exhaust pipe is arranged on the collecting tank, and the gas outlet end of the second exhaust pipe extends into the waste gas treatment tank; the water tank is arranged on one side of the waste gas treatment tank, which is far away from the collecting tank; the water cooling device is arranged on the water tank.
Preferably, the water cooling device comprises a water pump, a water suction pipe, a water inlet pipe, a water return pipe, a cooling coil pipe and a fan, the water pump is fixedly mounted at the top of the water tank, the water suction pipe is fixedly mounted on the inner wall of the top of the water tank, the water inlet end of the water suction pipe extends to the bottom end of the water tank, the water outlet end of the water suction pipe is fixedly connected with the water inlet end of the water pump, the water inlet pipe is fixedly mounted at one side of the cooling tank far away from the support plate, the water return pipe is located below the water inlet pipe, the water outlet end of the water return pipe is fixedly connected with the water tank, the cooling coil pipe is arranged in the water tank, and the air inlet end and the air outlet end of the cooling coil pipe both extend out of the water, the fan is fixedly installed on one side, far away from the waste gas treatment tank, of the water tank, and the air inlet end of the cooling coil is fixedly connected with the air outlet end of the fan.
Preferably, one side fixed mounting that the waste gas treatment jar was kept away from to the water tank has the moisturizing pipe, the moisturizing pipe is located the top of fan, be provided with the valve on the moisturizing pipe.
Preferably, the top of the evaporating pot is provided with an opening, a first sealing cover is arranged in the opening at the top of the evaporating pot, the first sealing cover is matched with the opening, and the bottom of the evaporating pot is provided with a heating groove.
Preferably, the top of the collection tank is provided with an opening, a second sealing cover is arranged in the opening in the top of the collection tank, the second sealing cover is matched with the opening, and the dropping liquid pipe and the second exhaust pipe penetrate through the second sealing cover.
Preferably, the top of exhaust-gas treatment jar is the opening, the bottom fixed mounting of backup pad has four supporting legs, four the supporting leg is the rectangular array and distributes.
Compared with the prior art, the utility model provides a hydrochloric acid production process enrichment facility has following beneficial effect:
the utility model provides a hydrochloric acid production process enrichment facility, this device not only make hydroenergy constant temperature as far as possible cool off steam through the mode that the circulating water is many, and comparatively environmental protection has prevented the entering of outside impurity again simultaneously, and protect equipment, through cooling coil increased with the contact surface of water and the temperature of different positions, the cooling effect is good.
Drawings
FIG. 1 is a schematic sectional view of a preferred embodiment of a hydrochloric acid production process concentration apparatus according to the present invention;
fig. 2 is a schematic sectional view of the concentrated coil pipe and the dropping pipe according to the present invention.
Reference numbers in the figures: 1. the utility model discloses a solar water heater, including backup pad, 2, evaporating pot, 3, cooling tank, 4, concentrated coil pipe, 5, first blast pipe, 6, collection tank, 7, dropping liquid pipe, 8, exhaust-gas treatment jar, 9, second blast pipe, 10, water tank, 11, water pump, 12, the pipe that absorbs water, 13, inlet tube, 14, wet return, 15, cooling coil pipe, 16, fan.
Detailed Description
The present invention will be further described with reference to the accompanying drawings and embodiments.
Referring to fig. 1 and fig. 2, fig. 1 is a schematic sectional view of a hydrochloric acid production process concentration device according to a preferred embodiment of the present invention; fig. 2 is a schematic sectional view of the concentrated coil pipe and the dropping pipe according to the present invention. The hydrochloric acid production process enrichment facility includes: a support plate 1; the evaporation tank 2 is arranged on the support plate 1, and the top and the bottom of the evaporation tank 2 extend out of the support plate 1; the cooling tank 3 is fixedly arranged on one side of the supporting plate 1; the concentration coil 4 is arranged in the cooling tank 3, and the air inlet end and the air outlet end of the concentration coil 4 both extend out of the cooling tank 3; the first exhaust pipe 5 is fixedly installed on one side, close to the cooling tank 3, of the evaporation tank 2, the first exhaust pipe 5 is located above the evaporation tank 2, and the air outlet end of the first exhaust pipe 5 is connected with the air inlet end of the concentration coil pipe 4 in an inserted mode; a collection tank 6, the collection tank 6 being disposed below the cooling tank 3; the drip pipe 7 is arranged on the collecting tank 6, the top end of the drip pipe 7 extends out of the drip pipe 7, and the air inlet end of the drip pipe 7 is connected with the air outlet end of the concentration coil pipe 4 in an inserted manner; the waste gas treatment tank 8 is arranged on one side, away from the evaporation tank 2, of the collection tank 6, and the waste gas treatment tank 8 is arranged on the other side, away from the evaporation tank 2, of the collection tank 6; a second exhaust pipe 9, wherein the second exhaust pipe 9 is arranged on the collecting tank 6, and an air outlet end of the second exhaust pipe 9 extends into the waste gas treatment tank 8; a water tank 10, wherein the water tank 10 is arranged on one side of the waste gas treatment tank 8 far away from the collecting tank 6; and the water cooling device is arranged on the water tank 10.
The water cooling device comprises a water pump 11, a water suction pipe 12, a water inlet pipe 13, a water return pipe 14, a cooling coil 15 and a fan 16, wherein the water pump 11 is fixedly installed at the top of the water tank 10, the water suction pipe 12 is fixedly installed on the inner wall of the top of the water tank 10, the water inlet end of the water suction pipe 12 extends to the bottom end of the water tank 10, the water outlet end of the water suction pipe 12 is fixedly connected with the water inlet end of the water pump 11, the water inlet pipe 13 is fixedly installed at one side of the cooling tank 3 far away from the support plate 1, the water inlet end of the water inlet pipe 13 is fixedly connected with the water outlet end of the water pump 11, the water return pipe 14 is fixedly installed at one side of the cooling tank 3 far away from the support plate 1, the water return pipe 14 is located below the water inlet pipe 13, the water outlet end of the water return pipe 14 is fixedly connected with, the inlet end of cooling coil 15 all extends to with the end of giving vent to anger outside the water tank 10, fan 16 fixed mounting be in the water tank 10 is kept away from one side of exhaust-gas treatment jar 8, cooling coil 15's inlet end with fan 16's the end fixed connection of giving vent to anger.
One side fixed mounting that water tank 10 kept away from exhaust-gas treatment jar 8 has the moisturizing pipe, the moisturizing pipe is located fan 16's top, be provided with the valve on the moisturizing pipe.
The top of evaporating pot 2 is the opening, be equipped with first sealed lid in the open-top of evaporating pot 2, first sealed lid with opening looks adaptation, the heating bath has been seted up to the bottom of evaporating pot 2.
The top of collection tank 6 is the opening, be equipped with the sealed lid of second in the open-top of collection tank 6, the sealed lid of second with opening looks adaptation, dropping liquid pipe 7 with second blast pipe 9 all runs through the sealed lid of second.
The top of exhaust-gas treatment jar 8 is the opening, the bottom fixed mounting of backup pad 1 has four supporting legs, four the supporting leg is the rectangular array and distributes.
The utility model provides a hydrochloric acid production process enrichment facility's theory of operation as follows:
when the concentrated hydrochloric acid evaporator is used, a plurality of prepared stock solutions are respectively placed into an evaporating pot 2, a collecting pot 6 and a waste gas treatment pot 8, when concentration is carried out, the evaporating pot 2 is heated through a heating groove, a water pump 11 and a fan 16 are started simultaneously, the water pump 11 sucks water in a water tank 10 through a water suction pipe 12 and then discharges the water into a cooling pot 3 through a water inlet pipe 13, a concentration coil pipe 4 is cooled through the cooling pot 3 and then reenters the water tank 10 through a water return pipe 14, meanwhile, the fan 16 sucks external cold air and then enters a cooling coil pipe 15, hot air in the water tank 10 is absorbed through the cooling coil pipe 15 and then discharges the air to cool the water in the water tank 10, when the stock solutions in the evaporating pot 2 are heated and evaporated, the stock solutions enter the concentration coil pipe 4 through a first exhaust pipe 5, at the moment, steam rainwater in the concentration coil pipe 4 is cooled to form water drops, and then the water drops enter the collecting pot 6 through a, unnecessary waste gas is led into in the exhaust-gas treatment jar 8 through second blast pipe 9, takes place the neutralization with the aqueous ammonia in the exhaust-gas treatment jar 8, and it is to be noted that second blast pipe 9 is located the top of aqueous ammonia, can not be stained with the aqueous ammonia.
Compared with the prior art, the utility model provides a hydrochloric acid production process enrichment facility has following beneficial effect:
the utility model provides a hydrochloric acid production process enrichment facility, this device not only make hydroenergy constant temperature as far as possible cool off steam through the mode that the circulating water is many, and comparatively environmental protection again simultaneously, sealed water tank 10 has prevented the entering of outside impurity, protects equipment, has increased the temperature with the contact surface of water and different positions through cooling coil 15, and the cooling effect is good.
It should be noted that the device structure and the accompanying drawings of the present invention mainly describe the principle of the present invention, and in the technology of this design principle, the settings of the power mechanism, the power supply system, the control system, etc. of the device are not completely described, and the details of the power mechanism, the power supply system, and the control system can be clearly known on the premise that those skilled in the art understand the principle of the present invention.
The above only is the embodiment of the present invention, not limiting the scope of the present invention, all the equivalent structures or equivalent processes of the present invention are used in the specification and the attached drawings, or directly or indirectly applied to other related technical fields, and the same principle is included in the protection scope of the present invention.
Claims (6)
1. A hydrochloric acid production process enrichment facility which characterized in that includes:
a support plate;
the evaporation tank is arranged on the supporting plate, and the top and the bottom of the evaporation tank extend out of the supporting plate;
the cooling tank is fixedly arranged on one side of the supporting plate;
the concentration coil is arranged in the cooling tank, and the air inlet end and the air outlet end of the concentration coil extend out of the cooling tank;
the first exhaust pipe is fixedly installed on one side, close to the cooling tank, of the evaporation tank, the first exhaust pipe is located above the evaporation tank, and the air outlet end of the first exhaust pipe is connected with the air inlet end of the concentration coil pipe in an inserted mode;
a collection tank disposed below the cooling tank;
the drip pipe is arranged on the collecting tank, the top end of the drip pipe extends out of the drip pipe, and the air inlet end of the drip pipe is spliced with the air outlet end of the concentration coil pipe;
the waste gas treatment tank is arranged on one side of the collecting tank, which is far away from the evaporation tank;
the second exhaust pipe is arranged on the collecting tank, and the gas outlet end of the second exhaust pipe extends into the waste gas treatment tank;
the water tank is arranged on one side of the waste gas treatment tank, which is far away from the collecting tank;
the water cooling device is arranged on the water tank.
2. The hydrochloric acid production process concentrating device according to claim 1, wherein the water cooling device comprises a water pump, a water suction pipe, a water inlet pipe, a water return pipe, a cooling coil and a fan, the water pump is fixedly installed at the top of the water tank, the water suction pipe is fixedly installed on the inner wall of the top of the water tank, the water inlet end of the water suction pipe extends to the bottom end of the water tank, the water outlet end of the water suction pipe is fixedly connected with the water inlet end of the water pump, the water inlet pipe is fixedly installed at one side of the cooling tank far away from the supporting plate, the water inlet end of the water inlet pipe is fixedly connected with the water outlet end of the water pump, the water return pipe is fixedly installed at one side of the cooling tank far away from the supporting plate, the water return pipe is located below the water inlet pipe, the water outlet end of the water return pipe is fixedly connected with, the inlet end of cooling coil and the end of giving vent to anger all extend to outside the water tank, fan fixed mounting is in the water tank is kept away from one side of exhaust-gas treatment jar, cooling coil's inlet end with the end fixed connection of giving vent to anger of fan.
3. The hydrochloric acid production process concentrating device according to claim 2, wherein a water replenishing pipe is fixedly installed on one side of the water tank, which is far away from the waste gas treatment tank, the water replenishing pipe is located above the fan, and a valve is arranged on the water replenishing pipe.
4. The hydrochloric acid production process concentrating device of claim 1, wherein the top of the evaporation tank is an opening, a first sealing cover is arranged in the opening of the top of the evaporation tank, the first sealing cover is matched with the opening, and a heating groove is formed in the bottom of the evaporation tank.
5. The hydrochloric acid production process concentrating device of claim 1, wherein the top of the collecting tank is an opening, a second sealing cover is arranged in the opening of the top of the collecting tank, the second sealing cover is matched with the opening, and the dropping liquid pipe and the second exhaust pipe both penetrate through the second sealing cover.
6. The hydrochloric acid production process concentrating device of claim 1, wherein the top of the waste gas treatment tank is open, and four support legs are fixedly mounted at the bottom of the support plate and distributed in a rectangular array.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020301873.7U CN212467147U (en) | 2020-03-12 | 2020-03-12 | Hydrochloric acid production process enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020301873.7U CN212467147U (en) | 2020-03-12 | 2020-03-12 | Hydrochloric acid production process enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN212467147U true CN212467147U (en) | 2021-02-05 |
Family
ID=74416092
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202020301873.7U Expired - Fee Related CN212467147U (en) | 2020-03-12 | 2020-03-12 | Hydrochloric acid production process enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN212467147U (en) |
-
2020
- 2020-03-12 CN CN202020301873.7U patent/CN212467147U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20211213 Address after: 100000 No. 027, 10 / F, block B, building 3, Haidian Street, Haidian District, Beijing Patentee after: Beijing Silicon porcelain Xinneng Technology Co.,Ltd. Address before: No. 425, unit 1101 and 1102, No. 374-2, Beijing Road, Yuexiu District, Guangzhou, Guangdong 510000 Patentee before: Yang Lanying |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20210205 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |