CN216572460U - Shipborne energy-saving emission-reducing processing device - Google Patents
Shipborne energy-saving emission-reducing processing device Download PDFInfo
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- CN216572460U CN216572460U CN202123344354.2U CN202123344354U CN216572460U CN 216572460 U CN216572460 U CN 216572460U CN 202123344354 U CN202123344354 U CN 202123344354U CN 216572460 U CN216572460 U CN 216572460U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract
The utility model provides a ship-borne energy-saving emission-reducing processing device, belonging to the technical field of ships; including spraying the jar, it is equipped with gas inlet pipe and sprays the inlet tube to spray the jar, it has the spray pump to spray the inlet tube connection, the spray pump is connected with spray outlet pipe, spray outlet pipe is equipped with the shower nozzle, it is equipped with heat transfer water jacket and gas outlet pipe to spray the jar, gas outlet pipe is connected with the heat exchanger, the heat exchanger is connected with the activated carbon case, the activated carbon case is connected with the fan, the fan is equipped with the evacuation pipe, it is equipped with the circulation water pitcher to spray the jar, the circulation water pitcher is connected with heat transfer cover circulating pump and heat exchanger circulating pump, heat transfer cover circulating pump is connected to the heat transfer water jacket, the heat transfer water jacket is connected to the circulation water pitcher, the heat exchanger circulating pump is connected to the heat exchanger, the heat exchanger is connected to the circulation water pitcher. The utility model discloses a circulation sprays alkaline solution and gets rid of sulfur dioxide and nitrogen oxide wherein to retrieve as boats and ships life hot water its heat, reach the energy saving and reduce the purpose of emission.
Description
Technical Field
The utility model provides a ship-borne energy saving and emission reduction processing apparatus belongs to boats and ships technical field.
Background
In world freight transportation, ocean transportation occupies a large proportion. The ocean cargo transportation has the characteristics of large traffic capacity, large transportation volume, low transportation cost, strong adaptability to cargos, low speed, high risk and the like. At present, more than two thirds of the total freight volume of international trade, 90% of the total freight volume of import and export goods in China are transported by ocean. With the rapid increase of the number of transport ships, pollution and harm of pollutants discharged by ships to the atmospheric environment and the marine environment are becoming more and more serious. The tail gas discharged by the combustion of the marine diesel engine is mainly sulfur dioxide SO2And nitrogen oxide NO2Mainly, according to the statistical data of 2014 International Maritime Organization (IMO), the annual SO emission of ship tail gas is shown2、NO2Accounting for about 13% and 15% of the total global emissions, respectively. The related report also indicates that the air pollution caused by the ship exhaust gas accounts for about 5-11% of the total air pollution. The exhaust gas generated by the marine diesel engine needs to remove pollutants sulfur dioxide and nitrogen oxide in the exhaust gas, and the exhaust gas discharged by the marine diesel engine has high temperature and needs to be further cooled.
SUMMERY OF THE UTILITY MODEL
The utility model provides a ship-borne energy saving and emission reduction processing apparatus adopts the circulation to spray alkaline solution and gets rid of sulfur dioxide and nitrogen oxide wherein to retrieve as boats and ships life hot water its heat, reach the purpose that the energy saving reduces the emission.
The utility model provides a ship-borne energy saving and emission reduction processing apparatus, its characterized in that: the spraying device comprises a spraying tank, wherein the spraying tank is provided with a gas inlet pipe, the bottom of the spraying tank is provided with a spraying inlet pipe, the spraying inlet pipe is connected with a spraying pump, the spraying pump is connected with a spraying outlet pipe, the spraying outlet pipe is inserted into the spraying tank, the spraying outlet pipe is positioned in the spraying tank and is provided with a spray head, the outer wall of the spraying tank is sleeved with a heat exchange water jacket, the top of the spraying tank is provided with a gas outlet pipe, the gas outlet pipe is connected with a heat exchanger tube side, the other end of the heat exchanger tube side is connected with an activated carbon box through a pipeline, one end of the activated carbon box is connected with a fan through a pipeline, an exhaust pipe is arranged at the outlet of the fan, a circulating water tank is arranged outside the spraying tank, the circulating water tank is connected with a heat exchange sleeve circulating pump and a heat exchanger circulating pump through pipelines, the heat exchange sleeve circulating pump is connected to the bottom of the heat exchange water jacket through a pipeline, the top of the heat exchange water jacket is connected to the circulating water tank through a pipeline, the heat exchanger circulating pump is connected to the heat exchanger shell pass through a pipeline, and the other end of the heat exchanger shell pass is connected to the circulating water tank through a pipeline.
The inner side upper portion of the spraying tank is provided with a demister, the outer side upper portion of the spraying tank is provided with an alkali supplementing pipe, the alkali supplementing pipe is provided with an alkali supplementing valve, and the spraying tank is provided with a first liquid level meter.
The spray outlet pipe has the sewage treatment pipe through three way connection, the sewage treatment pipe is equipped with the sewage valve, the sewage treatment union coupling has sewage treatment plant, sewage treatment plant is equipped with row sediment pipe, row sediment union coupling has row sediment jar, sewage treatment plant is equipped with the water purification pipe, the water purification union coupling has the water purification backwash pump, the water purification backwash pump passes through pipe connection to circulation water pitcher.
The circulating water tank is provided with a second liquid level meter, the circulating water tank is provided with a water supplementing pipe, and the water supplementing pipe is provided with a water supplementing valve.
The outlet of the heat exchange sleeve circulating pump is connected with a spray tank water replenishing pipe through a tee joint, the spray tank water replenishing pipe is connected to a spray outlet pipe, and the spray tank water replenishing pipe is provided with a spray tank water replenishing valve.
The inlet tube of heat exchanger circulating pump is equipped with thermometer one, the outlet pipe of heat exchanger circulating pump has the hot-water line through the tee junction, the hot-water line is equipped with the hot water valve, hot-water line end-to-end connection has the hot water storage tank, hot water storage tank outer wall has twined the electric heating coil pipe, hot water storage tank outside parcel has the heat preservation, the electric heating coil pipe parcel is inside the heat preservation, hot water storage tank top is equipped with the relief valve, there is the hot water circulating pump hot water storage tank bottom through the tube coupling, the hot water circulating pump export is connected to hot water storage tank top through the pipeline, the inlet tube of hot water circulating pump is equipped with thermometer two, the outlet pipe of hot water circulating pump has the hot water delivery pipe through the tee junction, the hot water delivery pipe is equipped with the hot water feed valve.
The activated carbon box is filled with activated carbon.
The spraying inlet pipe is provided with a PH meter.
The principle of the utility model is as follows:
the alkaline solution reacts with nitrogen oxides: 2NO2+2OH—＝NO3 —+NO2 —+H2O
Reacting the alkaline solution with sulfur dioxide: SO (SO)2+2OH—＝SO3 2—+H2O
When the device is used, firstly, the water replenishing valve is opened, water is replenished to the circulating water tank through the water replenishing pipe, the water replenishing level of the liquid level meter II is observed, the heat exchange sleeve circulating pump is started after water replenishing is finished, water in the circulating water tank is pumped to the heat exchange water jacket through the heat exchange sleeve circulating pump and then flows back to the circulating water tank from the top of the heat exchange water jacket, cold water circulation of the heat exchange water jacket is realized, the heat exchange water jacket is started, the water in the circulating water tank is pumped to the heat exchanger shell pass through the heat exchanger circulating pump and then flows back to the circulating water tank from the other end of the heat exchanger shell pass, cold water circulation of the heat exchanger shell pass is realized, the water replenishing valve of the spray tank is opened, water replenishing is performed to the spray tank through the heat exchange sleeve circulating pump, a certain water amount is replenished by the observation liquid level meter I, the liquid level of the circulating water tank at the moment correspondingly descends, water is continuously replenished to the circulating water tank through the water tank by the observation liquid level meter II opening water replenishing valve, the spray tank, the spray pump is started after water replenishing is completed, the water replenishing pipe, the water in the spray tank is sprayed, the liquid level meter II is sprayed, the circulating water is sprayed, and then the circulating water is sprayed, and then is sprayed, and the circulating water is sprayed, and then the circulating water is sprayed, and then is sprayed, and the water is discharged, and then the water is discharged, and then is discharged, and discharged, The spray pump and the spray outlet pipe are atomized by the spray nozzle and then return to the spray tank, self circulation of spray water in the spray tank is realized, an alkali supplement valve is opened, alkali liquor is introduced into the spray tank through an alkali supplement pipe, the PH value of the spray tank is adjusted through display of a PH meter, waste gas is introduced through a gas inlet pipe after adjustment is completed, the fan is started at the same time, the waste gas enters the spray tank and contacts with alkaline vaporific solution sprayed by the spray nozzle to dissolve nitrogen oxide, sulfur dioxide, dust and other impurities in the gas, the waste gas is rapidly cooled, the waste gas continues to pass through a demister to remove water mist carried in the gas, the waste gas continues to pass through a heat exchanger which carries out secondary deep cooling on the waste gas, the cooled waste gas passes through an activated carbon box to further remove a small amount of residual nitrogen oxide, sulfur dioxide, dust and other impurities, clean low-temperature gas enters an emptying pipe through the fan to be exhausted to the atmosphere along with the proceeding of reaction and heat exchange, the temperature of water in the spraying tank slowly rises, the temperature of water in the spraying tank is reduced through heat exchange with the heat exchange water jacket, the PH value in the spraying tank continuously falls along with reaction, the PH value in the spraying tank is maintained through observing the supplement of alkali liquor by a PH meter, the temperature of water in the circulating tank continuously rises along with the continuous heat exchange temperature, observing a first thermometer, if the temperature is too high, opening a hot water valve, enabling high-temperature water in the circulating tank to enter a hot water pipe through a heat exchanger circulating pump, and finally entering a hot water storage tank, simultaneously opening a water supplement valve to supplement cold water for the circulating tank to reduce the temperature in the circulating tank for continuous heat exchange, starting the hot water circulating pump after the hot water storage tank enters water, automatically circulating the hot water storage tank, arranging a second thermometer on a water pipe at the bottom of the hot water storage tank to display the temperature of the hot water storage tank, and starting an electric heating coil pipe to heat the hot water storage tank when the temperature of the hot water tank is lower than the required temperature of domestic hot water, and controlling the temperature in the hot water storage tank through the thermometers and the electric heating coil, if the downstream has hot water demand, open the hot water supply valve, deliver hot water to the demand equipment through the hot water delivery pipe. Along with the reaction, the waste residue content in the spraying tank is higher and higher, and the sewage valve is regularly opened, and the sewage in the spraying tank is replaced through the sewage treatment pipe and is discharged to the sewage treatment device, and the waste residue that sewage treatment was accomplished is discharged to the scum discharging tank, and the water purification that the processing was accomplished is carried to the circulation water pitcher through the water purification backwash pump. The safety valve is used for preventing the pressure in the hot water storage tank from being overhigh, and the heat preservation layer is used for ensuring that the heat in the hot water storage tank is not dissipated.
The utility model has the advantages that:
the utility model provides a ship-borne energy saving and emission reduction processing apparatus adopts the circulation to spray alkaline solution and gets rid of sulfur dioxide and nitrogen oxide wherein to retrieve as boats and ships life hot water its heat, reach the purpose that the energy saving reduces the emission.
Drawings
Fig. 1 is a schematic structural view of the ship-borne energy-saving emission-reducing processing device of the utility model.
(1, spray tank, 2, gas inlet pipe, 3, spray inlet pipe, 4, spray pump, 5, spray outlet pipe, 6, spray head, 7, heat exchange water jacket, 8, gas outlet pipe, 9, heat exchanger, 10, activated carbon box, 11, blower, 12, emptying pipe, 13, circulation water tank, 14, heat exchange jacket circulation pump, 15, heat exchanger circulation pump, 16, demister, 17, alkali supplement pipe, 18, alkali supplement valve, 19, level gauge I, 20, sewage treatment pipe, 21, sewage valve, 22, sewage treatment device, 23, slag discharge pipe, 24, slag discharge tank, 25, water purification pipe, 26, water purification reflux pump, 27, level gauge II, 28, water supplement pipe, 29, water supplement valve, 30, spray tank water supplement pipe, 31, spray tank water supplement valve, 32, thermometer I, 33, hot water pipe, 34, hot water valve, 35, hot water storage tank, 36, electric heating coil, 37, heat preservation layer, 38, heat exchanger, 10, hot water valve, 35, hot water pipe, hot water storage tank, 23, hot water storage tank, 18, hot water storage tank, 18, hot water storage tank, 18, and hot water storage tank, 18, hot water storage tank, hot water storage, 18, hot water storage tank, hot water storage tank, hot water, Safety valve 39, hot water circulating pump 40, thermometer II, 41, hot water supply pipe 42, hot water supply valve 43, active carbon 44, PH meter)
Detailed Description
The present invention will be further explained with reference to the accompanying drawings.
The utility model provides a ship-borne energy saving and emission reduction processing apparatus, its characterized in that: the spraying device comprises a spraying tank 1, wherein a gas inlet pipe 2 is arranged on the spraying tank 1, a spraying inlet pipe 3 is arranged at the bottom of the spraying tank 1, the spraying inlet pipe 3 is connected with a spraying pump 4, the spraying pump 4 is connected with a spraying outlet pipe 5, the spraying outlet pipe 5 is inserted into the spraying tank 1, the spraying outlet pipe 5 is positioned inside the spraying tank 1 and is provided with a nozzle 6, a heat exchange water jacket 7 is sleeved on the outer wall of the spraying tank 1, a gas outlet pipe 8 is arranged at the top of the spraying tank 1, the gas outlet pipe 8 is connected with a heat exchanger 9 tube pass, the other end of the heat exchanger 9 tube pass is connected with an activated carbon box 10 through a pipeline, one end of the activated carbon box 10 is connected with a fan 11 through a pipeline, an emptying pipe 12 is arranged at the outlet of the fan 11, a circulating water tank 13 is arranged outside the spraying tank 1, the circulating water tank 13 is connected with a heat exchange water jacket circulating pump 14 and a heat exchanger circulating pump 15 through a pipeline, the heat exchange jacket circulating pump 14 is connected to the bottom of the heat exchange water jacket 7 through a pipeline, the top of the heat exchange water jacket 7 is connected to the circulating water tank 13 through a pipeline, the heat exchanger circulating pump 15 is connected to the shell pass of the heat exchanger 9 through a pipeline, and the other end of the shell pass of the heat exchanger 9 is connected to the circulating water tank 13 through a pipeline.
The spray tank 1 inboard upper portion is equipped with defroster 16, spray tank 1 outside upper portion is equipped with mends alkali pipe 17, mend alkali pipe 17 and be equipped with mends alkali valve 18, spray tank 1 is equipped with level gauge 19.
The spray outlet pipe 5 has sewage treatment pipe 20 through the three way connection, sewage treatment pipe 20 is equipped with bilge valve 21, sewage treatment pipe 20 is connected with sewage treatment device 22, sewage treatment device 22 is equipped with row's sediment pipe 23, row's sediment pipe 23 is connected with row's sediment jar 24, sewage treatment device 22 is equipped with clean water pipe 25, clean water pipe 25 is connected with water purification backwash pump 26, water purification backwash pump 26 passes through pipe connection to circulation water tank 13.
The circulating water tank 13 is provided with a second liquid level meter 27, the circulating water tank 13 is provided with a water supplementing pipe 28, and the water supplementing pipe 28 is provided with a water supplementing valve 29.
The outlet of the heat exchange sleeve circulating pump 14 is connected with a spraying tank water replenishing pipe 30 through a tee joint, the spraying tank water replenishing pipe 30 is connected to the spraying outlet pipe 5, and the spraying tank water replenishing pipe 30 is provided with a spraying tank water replenishing valve 31.
The inlet tube of heat exchanger circulating pump 15 is equipped with thermometer 32, the outlet pipe of heat exchanger circulating pump 15 has hot water pipe 33 through the tee junction, hot water pipe 33 is equipped with hot water valve 34, hot water pipe 33 end-to-end connection has hot water storage tank 35, hot water storage tank 35 outer wall is twined electric heating coil 36, hot water storage tank 35 outside parcel has heat preservation 37, electric heating coil 36 parcel is inside heat preservation 37, hot water storage tank 35 top is equipped with relief valve 38, there is hot water circulating pump 39 hot water storage tank 35 bottom through the tube coupling, hot water circulating pump 39 exports through tube coupling to hot water storage tank 35 top, hot water circulating pump 39's inlet tube is equipped with thermometer two 40, hot water circulating pump 39's outlet pipe has hot water supply pipe 41 through the tee junction, hot water supply pipe 41 is equipped with hot water supply valve 42.
The activated carbon box 10 is filled with activated carbon 43.
The spray inlet pipe 3 is provided with a PH meter 44.
According to the illustration of FIG. 1:
the alkaline solution reacts with nitrogen oxides: 2NO2+2OH—＝NO3 —+NO2 —+H2O
Reacting the alkaline solution with sulfur dioxide: SO (SO)2+2OH—＝SO3 2—+H2O
When the device is used, firstly, the water replenishing valve 29 is opened, water is replenished to the circulating water tank 13 through the water replenishing pipe 28, the replenishing water level of the second liquid level meter 27 is observed, the heat exchange sleeve circulating pump 14 is started after water replenishing is finished, water in the circulating water tank 13 is pumped to the heat exchange water jacket 7 through the heat exchange sleeve circulating pump 14 and then flows back to the circulating water tank 13 from the top of the heat exchange water jacket 7, cold water circulation of the heat exchange water jacket 7 is realized, the heat exchanger circulating pump 15 is started, water in the circulating water tank 13 is pumped to the shell pass of the heat exchanger 9 through the heat exchanger circulating pump 15, then flows back to the circulating water tank 13 from the other end of the shell pass of the heat exchanger 9, shell pass cold water circulation of the heat exchanger 9 is realized, the water replenishing valve 31 of the spraying tank is opened, water is replenished to the spraying tank 1 through the heat exchange sleeve circulating pump 14, a certain water amount of the first liquid level meter 19 is observed to be replenished, at the corresponding decline of the liquid level of the circulating water tank 13, the water replenishing valve 29 is opened through the second liquid level meter 27 to continue to replenish water to the circulating water tank 13, after the water supplement of the spraying tank 1 is completed, the spraying pump 4 is started, the water in the spraying tank 1 passes through the spraying inlet pipe 3, the spraying pump 4 and the spraying outlet pipe 5 and finally returns to the spraying tank 1 after being atomized by the spray head 6, the self circulation of the spraying water in the spraying tank 1 is realized, the alkali supplement valve 18 is opened, alkali liquor is introduced into the spraying tank 1 through the alkali supplement pipe 17, the PH value of the spraying tank 1 is displayed and adjusted through the PH meter 44, waste gas is introduced through the gas inlet pipe 2 after the adjustment is completed, the fan 11 is simultaneously started, the waste gas enters the spraying tank 1 and contacts with alkaline vaporific solution sprayed by the spray head 6, the impurities such as nitrogen oxide, sulfur dioxide, dust and the like in the dissolved gas are rapidly cooled, the waste gas continuously passes through the demister 16, the water mist carried in the gas is removed, the waste gas continuously passes through the heat exchanger 9, the heat exchanger 9 carries out secondary deep cooling on the waste gas, the cooled waste gas passes through the activated carbon tank 10, further removing a small amount of residual impurities such as nitrogen oxide, sulfur dioxide and dust, discharging clean low-temperature gas into an emptying pipe 12 through a fan 11 to atmosphere, along with the proceeding of reaction and heat exchange, slowly raising the water temperature in the spraying tank 1, reducing the water temperature in the spraying tank 1 through heat exchange with a heat exchange water jacket 7, continuously lowering the pH value in the spraying tank 1 along with the proceeding of reaction, maintaining the pH value in the spraying tank 1 by observing the alkali liquor supplemented by a pH meter 44, continuously raising the water temperature in the circulating water tank 13 along with the continuous heat exchange temperature, observing a first thermometer 32, if the temperature is too high, opening a hot water valve 34, enabling high-temperature water in the circulating water tank 13 to enter a hot water pipe 33 through a heat exchanger circulating pump 15, finally entering a hot water storage tank 35, simultaneously opening a water supplementing valve 29 to supplement cold water for the circulating water tank 13 to reduce the temperature in the circulating water tank 13 to continuously exchange, starting the hot water circulating pump 39 after the hot water storage tank 35 enters water, from circulation hot water storage tank 35, hot water storage tank 35 bottom water pipe is equipped with two 40 thermometers and shows hot water storage tank 35 temperature, if hot water storage tank 35 temperature is less than life hydrothermal demand temperature when, starts electric heating coil 36 and heats up for hot water storage tank 35, through two 40 thermometers and electric heating coil 36 control hot water storage tank 35 in the temperature, if the low reaches have the hot water demand when, opens hot water supply valve 42, carries hot water to demand device through hot water supply pipe 41. Along with the reaction, the content of the waste residue in the spraying tank 1 is higher and higher, the sewage valve 21 is opened periodically, the sewage in the spraying tank 1 is replaced through the sewage treatment pipe 20 and is discharged to the sewage treatment device 22, the waste residue after sewage treatment is discharged to the residue discharge tank 24, and the treated purified water is conveyed to the circulating water tank 13 through the purified water return pump 26. The safety valve 38 is used for preventing the pressure in the hot water storage tank 35 from being too high, and the insulating layer 37 is used for ensuring that the heat in the hot water storage tank 35 is not dissipated.
The utility model discloses a circulation sprays alkaline solution and gets rid of sulfur dioxide and nitrogen oxide wherein to retrieve as boats and ships life hot water its heat, reach the purpose that the energy saving reduces the emission.
Although the present invention has been described with reference to the preferred embodiments, it should be understood that various changes and modifications can be made by those skilled in the art without departing from the spirit and scope of the invention.
Claims (8)
1. The utility model provides a ship-borne energy saving and emission reduction processing apparatus which characterized in that: comprises a spraying tank (1), wherein the spraying tank (1) is provided with a gas inlet pipe (2), the bottom of the spraying tank (1) is provided with a spraying inlet pipe (3), the spraying inlet pipe (3) is connected with a spraying pump (4), the spraying pump (4) is connected with a spraying outlet pipe (5), the spraying outlet pipe (5) is inserted into the spraying tank (1), the spraying outlet pipe (5) is positioned inside the spraying tank (1) and is provided with a spray head (6), the outer wall of the spraying tank (1) is sleeved with a heat exchange water jacket (7), the top of the spraying tank (1) is provided with a gas outlet pipe (8), the gas outlet pipe (8) is connected with a heat exchanger (9), the gas outlet pipe (8) is connected with a pipe pass of the heat exchanger (9), the other end of the pipe pass of the heat exchanger (9) is connected with an activated carbon box (10) through a pipeline, one end of the activated carbon box (10) is connected with a fan (11) through a pipeline, the utility model discloses a heat exchanger, including fan (11), spray tank (1), circulation water tank (13), there are heat exchange cover circulating pump (14) and heat exchanger circulating pump (15) in fan (11) export, spray tank (1) outside and be equipped with circulation water tank (13), circulation water tank (13) have heat exchange cover circulating pump (14) and heat exchanger circulating pump (15) through the tube coupling, heat exchange cover circulating pump (14) are through tube coupling to heat exchange water jacket (7) bottom, tube coupling to circulation water tank (13) is passed through at heat exchange water jacket (7) top, heat exchanger circulating pump (15) are through tube coupling to heat exchanger (9) shell side, heat exchanger (9) shell side other end is through tube coupling to circulation water tank (13).
2. The shipborne energy-saving emission-reducing processing device according to claim 1, characterized in that: spray jar (1) inboard upper portion and be equipped with defroster (16), spray jar (1) outside upper portion and be equipped with benefit alkali pipe (17), it is equipped with benefit alkali valve (18) to mend alkali pipe (17), spray jar (1) and be equipped with level gauge (19).
3. The shipborne energy-saving emission-reducing processing device according to claim 1, characterized in that: spray outlet pipe (5) and have sewage treatment pipe (20) through the three way connection, sewage treatment pipe (20) are equipped with bilge valve (21), sewage treatment pipe (20) are connected with sewage treatment device (22), sewage treatment device (22) are equipped with row sediment pipe (23), row sediment pipe (23) are connected with row sediment jar (24), sewage treatment device (22) are equipped with water purification pipe (25), water purification pipe (25) are connected with water purification backwash pump (26), water purification backwash pump (26) are through tube coupling to circulation water tank (13).
4. The shipborne energy-saving emission-reducing processing device according to claim 1, characterized in that: the circulating water tank (13) is provided with a second liquid level meter (27), the circulating water tank (13) is provided with a water supplementing pipe (28), and the water supplementing pipe (28) is provided with a water supplementing valve (29).
5. The shipborne energy-saving emission-reducing processing device according to claim 1, characterized in that: the outlet of the heat exchange sleeve circulating pump (14) is connected with a spray tank water replenishing pipe (30) through a tee joint, the spray tank water replenishing pipe (30) is connected to a spray outlet pipe (5), and the spray tank water replenishing pipe (30) is provided with a spray tank water replenishing valve (31).
6. The shipborne energy-saving emission-reducing processing device according to claim 1, characterized in that: the inlet pipe of the heat exchanger circulating pump (15) is provided with a first thermometer (32), the outlet pipe of the heat exchanger circulating pump (15) is connected with a hot water pipe (33) through a tee joint, the hot water pipe (33) is provided with a hot water valve (34), the tail end of the hot water pipe (33) is connected with a hot water storage tank (35), the outer wall of the hot water storage tank (35) is wound with an electric heating coil pipe (36), the outer side of the hot water storage tank (35) is wrapped with a heat insulation layer (37), the electric heating coil pipe (36) is wrapped inside the heat insulation layer (37), the top of the hot water storage tank (35) is provided with a safety valve (38), the bottom of the hot water storage tank (35) is connected with a hot water circulating pump (39) through a pipeline, the outlet of the hot water circulating pump (39) is connected to the top of the hot water storage tank (35) through a pipeline, the inlet pipe of the hot water circulating pump (39) is provided with a second thermometer (40), and the outlet pipe (41) of the hot water circulating pump (39) is connected through a tee joint, the hot water supply pipe (41) is provided with a hot water supply valve (42).
7. The shipborne energy-saving emission-reducing processing device according to claim 1, characterized in that: the interior of the activated carbon box (10) is filled with activated carbon (43).
8. The shipborne energy-saving emission-reducing processing device according to claim 1, characterized in that: the spraying inlet pipe (3) is provided with a PH meter (44).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123344354.2U CN216572460U (en) | 2021-12-28 | 2021-12-28 | Shipborne energy-saving emission-reducing processing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123344354.2U CN216572460U (en) | 2021-12-28 | 2021-12-28 | Shipborne energy-saving emission-reducing processing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216572460U true CN216572460U (en) | 2022-05-24 |
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ID=81629417
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202123344354.2U Active CN216572460U (en) | 2021-12-28 | 2021-12-28 | Shipborne energy-saving emission-reducing processing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216572460U (en) |
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2021
- 2021-12-28 CN CN202123344354.2U patent/CN216572460U/en active Active
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| CP01 | Change in the name or title of a patent holder |
Address after: 300459 Tianjin Binhai New Area Tianjin Binhai high tech Zone Tanggu marine science and Technology Park Xin'an Chuangye Plaza Building 8 d206 Patentee after: Tianjin Jingyan Technology Co.,Ltd. Address before: 300459 Tianjin Binhai New Area Tianjin Binhai high tech Zone Tanggu marine science and Technology Park Xin'an Chuangye Plaza Building 8 d206 Patentee before: Tianjin Tongyu Technology Development Co.,Ltd. |
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| CP01 | Change in the name or title of a patent holder |