CN216844643U - High-temperature condensate water recovery device - Google Patents
High-temperature condensate water recovery device Download PDFInfo
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- CN216844643U CN216844643U CN202123103995.9U CN202123103995U CN216844643U CN 216844643 U CN216844643 U CN 216844643U CN 202123103995 U CN202123103995 U CN 202123103995U CN 216844643 U CN216844643 U CN 216844643U
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Abstract
The utility model relates to a condensate recovery technical field, concretely relates to high temperature condensate recovery unit, including the recovery container, the recovery container upper end is connected with sealed lid, sealed covering has seted up water inlet and gas vent, be connected with inlet tube and steam discharge pipe on water inlet and the gas vent respectively, recovery container one side is connected with the outlet pipe, outlet valve and water pump have connected gradually on the outlet pipe, the outlet pipe communicates to the boiler room, the recovery container bottom is connected with the drain pipe, be equipped with the drain valve on the drain pipe. The utility model discloses enough draw the traditional chinese medicine and decoct and the high temperature comdenstion water that the concentration in-process produced to store in recovery vessel, store up the high temperature comdenstion water and let in the boiler and carry out the reutilization, practice thrift ion exchange boiler water consumption, the high temperature comdenstion water can directly let in the boiler simultaneously and use, and the temperature is high, has practiced thrift the ionized water heating time, practices thrift the use of natural gas simultaneously.
Description
Technical Field
The utility model relates to a condensate recovery technical field, concretely relates to high temperature condensate recovery unit.
Background
Traditional Chinese medicine is in the production process, it is common production processes to extract decocte and concentrate, and traditional Chinese medicine is extracting decocte and concentrate the in-process, probably 1.5 tons of steam are required to the hour, these steam can not directly be discharged because of the high temperature, need arrange into the sewer after the steam condensation, traditional processing method steam condensation time is long, cool off high temperature steam, the energy is wasted, the high temperature steam condensate water of more than 80 degrees can not be utilized, be unfavorable for energy-concerving and environment-protective, therefore, design a device that retrieves high temperature steam condensate water and just seem to be especially important.
Disclosure of Invention
The utility model discloses a solve the unable problem of recycling of high temperature comdenstion water, improved a high temperature comdenstion water recovery unit, the device can retrieve high temperature steam comdenstion water to heat, energy saving in the reuse high temperature comdenstion water.
In order to realize the purpose, the technical scheme of the utility model is that:
a high-temperature condensate water recovery device comprises a recovery container, wherein the upper end of the recovery container is connected with a sealing cover, the sealing cover is provided with a water inlet and an air outlet, the water inlet and the air outlet are respectively connected with a water inlet pipe and a hot air discharge pipe, one side of the recovery container is connected with a water outlet pipe, the water outlet pipe is sequentially connected with a water outlet valve and a water pump, the water outlet pipe is communicated to a boiler room, the bottom of the recovery container is connected with a water discharge pipe, and the water discharge pipe is provided with a water discharge valve;
the upper part of the recovery container is cylindrical, the lower part of the recovery container is funnel-shaped, the joint of the water outlet pipe and the recovery container is 5-10 cm higher than the cylindrical bottom, the water outlet pipe is connected with the funnel-shaped bottom, two liquid level detectors are arranged on the cylindrical inner wall of the recovery container, the two liquid level detectors are connected through a line, the line penetrates through a sealing cover and is connected with a control console, and the control console is connected with a water pump; the liquid level detector is respectively positioned above the joint of the water outlet pipe and the recovery container and 20-30 cm lower than the top of the recovery container, the outer wall of the recovery container is provided with a heat preservation layer, and the water inlet, the air outlet and the circuit penetrate through the sealing cover to be provided with sealing rings. Store up high temperature comdenstion water and let in the boiler and carry out the reutilization, practice thrift the water consumption of ion exchange boiler, high temperature comdenstion water can directly let in the boiler simultaneously and use, and the temperature is high, has practiced thrift ion water heating time, practices thrift the use of natural gas simultaneously.
Further, the device still includes the liquefaction container, inlet tube intercommunication recovery vessel and liquefaction container, liquefaction container upper portion is cylindrical, the lower part is for leaking hopper-shaped, the inlet tube is connected with the bottom that leaks hopper-shaped, the cylindrical centre is equipped with the division board, and the division board divides the liquefaction container into the ion water storage area on upper portion and the liquefaction district of lower part.
Furthermore, a thermometer is arranged in the ionized water storage area, the top of the side wall of the ionized water storage area is connected with an ionized water pipe, the bottom of the side wall of the ionized water storage area is connected with an ionized water outlet pipe, an electric valve is arranged on the ionized water outlet pipe, and the ionized water outlet pipe is communicated to a boiler room. The steam condensate water is liquefied and simultaneously the ionized water is heated, so that the energy required by heating the ionized water is saved, and meanwhile, the energy generated by liquefying the steam condensate water is fully utilized.
Furthermore, a steam pipe is connected to the side wall of the liquefaction area.
Further, the thermometer and the electric valve are both connected with a control console. The temperature of the ionized water can be observed conveniently, and the device can be conveniently introduced into a boiler room for use.
Furthermore, a pressure valve is arranged on the hot gas discharge pipe, so that the pressure in the recovery container is reduced.
Through the technical scheme, the beneficial effects of the utility model are that:
1. the utility model discloses can draw the high temperature comdenstion water that the decocte and the concentrated in-process produced with traditional chinese medicine and store in recovery vessel, store up the high temperature comdenstion water and let in the boiler and carry out the reutilization, practice thrift ion exchange boiler water consumption, the high temperature comdenstion water can directly let in the boiler simultaneously and use, and the temperature is high, has practiced thrift the ionized water heating time, practices thrift the use of natural gas simultaneously.
2. The utility model discloses a two liquid level detection wares detect high temperature comdenstion water level in the recovery container, and the liquid level detection ware detects and realizes the control to water pump switch through the control cabinet, prevents that the water pump from drawing water futilely when not having water in the recovery container, guarantees device stability.
The utility model discloses a separation molecule water and steam condensate water in the liquefaction container realize heating the ion water when the steam condensate water liquefaction, have practiced thrift the required energy of ion water heating, the energy that the liquefaction of make full use of steam condensate water produced simultaneously.
Drawings
Fig. 1 is a schematic structural diagram of the high-temperature condensate water recovery device of the present invention.
The reference numbers in the drawings are as follows: 1 is a recovery container, 2 is a heat preservation layer, 3 is a sealing cover, 4 is a water inlet pipe, 5 is a hot gas discharge pipe, 6 is a console, 7 is a liquid level detector, 8 is a water pump, 9 is a water outlet pipe, 10 is a water outlet valve, 11 is a water outlet pipe, 12 is a drain valve, 13 is a liquefaction container, 14 is an ionic water pipe, 15 is a steam pipe, 16 is an ionic water outlet pipe, 17 is an electric valve, 18 is a thermometer, and 19 is a pressure valve.
Detailed Description
The invention will be further explained with reference to the drawings and the detailed description below:
as shown in fig. 1, the high-temperature condensed water recovery device comprises a recovery container 1, wherein a sealing cover 3 is connected to the upper end of the recovery container 1, a water inlet and an air outlet are formed in the sealing cover 3, the water inlet and the air outlet are respectively connected with a water inlet pipe 4 and a hot gas discharge pipe 5, one side of the recovery container 1 is connected with a water outlet pipe 9, the water outlet pipe 9 is sequentially connected with a water outlet valve 10 and a water pump 8, the water outlet pipe 9 is communicated to a boiler room, the bottom of the recovery container 1 is connected with a water discharge pipe 11, and the water discharge pipe 11 is provided with a water discharge valve 12;
the upper part of the recovery container 1 is cylindrical, the lower part of the recovery container 1 is funnel-shaped, the joint of the water outlet pipe 9 and the recovery container 1 is 5-10 cm higher than the cylindrical bottom, the water outlet pipe 11 is connected with the funnel-shaped bottom, two liquid level detectors 7 are arranged on the cylindrical inner wall of the recovery container 1, the two liquid level detectors 7 are connected through a line, the line penetrates through the sealing cover 3 to be connected with a control console 6, and the control console 6 is connected with a water pump 8; the liquid level detector 7 is respectively positioned above the joint of the water outlet pipe 9 and the recovery container 1 and 20-30 cm lower than the top of the recovery container 1, the outer wall of the recovery container 1 is provided with a heat preservation layer 2, and the water inlet, the exhaust port and the line pass through the sealing cover 3 and are provided with sealing rings. High-temperature condensate water is introduced into the recovery container 1 through the water inlet pipe 4, steam generated by the high-temperature condensate water in the recovery container 1 is discharged from the hot gas discharge pipe 5, when the boiler needs to use the high-temperature condensate water, the water outlet valve 10 and the water pump 8 are opened, the high-temperature condensate water is introduced into the boiler for use, when the water level in the recovery container 1 is located on the liquid level detector 7 above the joint of the water outlet pipe 9 and the recovery container 1, the water pump 8 is closed by the console 6, the introduction of the high-temperature condensate water into the boiler is stopped, when the water level in the recovery container 1 rises to the liquid level detector 7 20-30 cm away from the top of the recovery container 1, the console 6 controls the water pump 8 to be started, the high-temperature condensate water continues to be introduced into the boiler, the secondary utilization of the condensate water is realized, the water consumption of the ion exchange boiler is saved, meanwhile, the high-temperature condensate water can be directly introduced into the boiler for use, the water temperature is high, the heating time of the ionized water is saved, and meanwhile, the natural gas is saved, when the natural gas is not used for a long time, the drain valve 12 is opened, and the condensed water cooled in the recovery container 1 is discharged out of the recovery container 1 through the drain pipe 11.
The device still includes liquefaction container 13, inlet tube 4 intercommunication recovery vessel 1 and liquefaction container 13, liquefaction container 13 upper portion is cylindrical, the lower part is for leaking hopper-shaped, inlet tube 4 is connected with leaking hopper-shaped bottom, be equipped with the division board in the middle of the cylindrical, the division board is divided into the ionic water storage area on upper portion and the liquefaction district of lower part with liquefaction container 13, be equipped with thermometer 18 in the ionic water storage area, ionic water storage area lateral wall top is connected with ionic water pipe 14, the bottom is connected with ionic water outlet pipe 16, be equipped with motorised valve 17 on the ionic water outlet pipe 16, ionic water outlet pipe 16 communicates to the boiler room, be connected with steam pipe 15 on the liquefaction district lateral wall, thermometer 18 and motorised valve 17 all are connected with control cabinet 6. Let in the ionized water in 14 to the ionized water storage areas through the ionized water pipe, let in the steam condensate water to the liquefaction district from steam pipe 15, steam condensate water and the ionized water in the ionized water storage area carry out the heat exchange, steam condensate water liquefaction enters into recovery vessel 1 from inlet tube 4 in, the ionized water is after heating to the uniform temperature, the thermometer can open motorised valve 17 through control cabinet 6, the ionized water lets in the boiler room and uses, the heat that utilizes the liquefaction of steam condensate water to produce heats the ionized water, practice thrift the required energy of ionized water heating, and is more energy-concerving and environment-protective.
The hot gas discharge pipe 5 is provided with a pressure valve 19, the high-temperature condensed water can generate steam in the recovery container 1, and when the pressure in the recovery container 1 reaches a certain pressure, the pressure can open the pressure valve 19 to discharge the steam, so that the pressure in the recovery container 1 is reduced.
When the device is used, ionized water is introduced into an ionized water storage area through the ionized water pipe 14, steam condensate water is introduced into a liquefaction area through the steam pipe 15, the steam condensate water exchanges heat with the ionized water in the ionized water storage area, the steam condensate water is liquefied and enters the recovery container 1 through the water inlet pipe 4, after the ionized water is heated to a certain temperature, the thermometer can open 17 through the control console 6, the ionized water is introduced into a boiler electric valve room for use, the ionized water is heated by utilizing heat generated by liquefying the steam condensate water, energy required by heating the ionized water is saved, energy is saved, the device is more energy-saving and environment-friendly, steam generated by high-temperature condensate water in the recovery container 1 increases the pressure in the recovery container 1, when a certain pressure intensity is reached in the recovery container 1, the pressure can open the pressure valve 19 to release the steam, the pressure intensity in the recovery container 1 is reduced, and when the boiler needs to use the high-temperature condensate water, the water outlet valve 10 and the water pump 8 are opened, use in letting in the boiler with high temperature comdenstion water, when the water level in recovery container 1 is located the liquid level detector 7 of outlet pipe 9 and recovery container 1 junction top, control cabinet 6 can close water pump 8, stop to let in high temperature comdenstion water to the boiler, when rising to the liquid level detector 7 of 20cm ~ 30cm departments apart from recovery container 1 top in recovery container 1, control cabinet 6 control water pump 8 starts, continue to let in high temperature comdenstion water to the boiler, realize the reutilization to the comdenstion water, practice thrift ion exchange boiler water consumption, high temperature comdenstion water can directly let in the boiler simultaneously and use, the temperature is high, the ionized water heating time has been practiced thrift, the use of natural gas is practiced thrift simultaneously, when not using for a long time, open drain valve 12, through drain pipe 11 with recovery container 1 in the comdenstion water that has cooled off recovery container 1.
The above-mentioned embodiments are merely preferred embodiments of the present invention, and are not intended to limit the scope of the present invention, so that all equivalent changes or modifications made by the technical solutions described in the claims of the present invention should be included in the claims of the present invention.
Claims (6)
1. The high-temperature condensate water recovery device comprises a recovery container (1), and is characterized in that the upper end of the recovery container (1) is connected with a sealing cover (3), the sealing cover (3) is provided with a water inlet and an air outlet, the water inlet and the air outlet are respectively connected with a water inlet pipe (4) and a hot air discharge pipe (5), one side of the recovery container (1) is connected with a water outlet pipe (9), the water outlet pipe (9) is sequentially connected with a water outlet valve (10) and a water pump (8), the water outlet pipe (9) is communicated with a boiler room, the bottom of the recovery container (1) is connected with a water discharge pipe (11), and the water discharge pipe (11) is provided with a water discharge valve (12);
the upper part of the recovery container (1) is cylindrical, the lower part of the recovery container is funnel-shaped, the joint of the water outlet pipe (9) and the recovery container (1) is 5-10 cm higher than the cylindrical bottom, the water outlet pipe (11) is connected with the funnel-shaped bottom, two liquid level detectors (7) are arranged on the cylindrical inner wall of the recovery container (1), the two liquid level detectors (7) are connected through a line, the line penetrates through the sealing cover (3) to be connected with a control console (6), and the control console (6) is connected with a water pump (8); the liquid level detector (7) is respectively positioned above the joint of the water outlet pipe (9) and the recovery container (1) and 20 cm-30 cm lower than the top of the recovery container (1), the outer wall of the recovery container (1) is provided with a heat preservation layer (2), and the water inlet, the exhaust port and the line are provided with sealing rings when passing through the sealing cover (3).
2. The high-temperature condensed water recovery device according to claim 1, further comprising a liquefaction container (13), wherein the water inlet pipe (4) is communicated with the recovery container (1) and the liquefaction container (13), the upper part of the liquefaction container (13) is cylindrical, the lower part of the liquefaction container is funnel-shaped, the water inlet pipe (4) is connected with the funnel-shaped bottom, a separation plate is arranged in the middle of the cylindrical shape, and the separation plate divides the liquefaction container (13) into an upper ionized water storage area and a lower liquefaction area.
3. The high-temperature condensed water recovery device according to claim 2, wherein a thermometer (18) is arranged in the ionized water storage area, the top of the side wall of the ionized water storage area is connected with an ionized water pipe (14), the bottom of the side wall of the ionized water storage area is connected with an ionized water outlet pipe (16), an electric valve (17) is arranged on the ionized water outlet pipe (16), and the ionized water outlet pipe (16) is communicated to a boiler room.
4. A high temperature condensate recovery apparatus according to claim 2, wherein a steam pipe (15) is connected to a sidewall of the liquefaction zone.
5. A high temperature condensate recovery device according to claim 3, characterized in that the thermometer (18) and the electric valve (17) are connected to the control console (6).
6. A high temperature condensate recovery device according to claim 1, characterized in that the hot gas discharge pipe (5) is provided with a pressure valve (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123103995.9U CN216844643U (en) | 2021-12-11 | 2021-12-11 | High-temperature condensate water recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123103995.9U CN216844643U (en) | 2021-12-11 | 2021-12-11 | High-temperature condensate water recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216844643U true CN216844643U (en) | 2022-06-28 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202123103995.9U Active CN216844643U (en) | 2021-12-11 | 2021-12-11 | High-temperature condensate water recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216844643U (en) |
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2021
- 2021-12-11 CN CN202123103995.9U patent/CN216844643U/en active Active
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