CN110550803A - Synthetic ammonia industry pollutant processing apparatus - Google Patents
Synthetic ammonia industry pollutant processing apparatus Download PDFInfo
- Publication number
- CN110550803A CN110550803A CN201910854310.2A CN201910854310A CN110550803A CN 110550803 A CN110550803 A CN 110550803A CN 201910854310 A CN201910854310 A CN 201910854310A CN 110550803 A CN110550803 A CN 110550803A
- Authority
- CN
- China
- Prior art keywords
- liquid
- synthetic ammonia
- pipe
- gas
- chamber
- 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.)
- Pending
Links
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims abstract description 80
- 229910021529 ammonia Inorganic materials 0.000 title claims abstract description 40
- 239000003344 environmental pollutant Substances 0.000 title claims abstract description 25
- 231100000719 pollutant Toxicity 0.000 title claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 153
- 238000003756 stirring Methods 0.000 claims abstract description 26
- 238000001914 filtration Methods 0.000 claims description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 29
- 238000006243 chemical reaction Methods 0.000 claims description 28
- 238000005192 partition Methods 0.000 claims description 16
- 238000005273 aeration Methods 0.000 claims description 13
- 239000002912 waste gas Substances 0.000 claims description 13
- 238000011084 recovery Methods 0.000 claims description 11
- 238000010438 heat treatment Methods 0.000 claims description 9
- 239000007789 gas Substances 0.000 claims description 8
- 230000005540 biological transmission Effects 0.000 claims description 5
- 238000001556 precipitation Methods 0.000 claims description 5
- 239000011148 porous material Substances 0.000 claims description 3
- 230000000903 blocking effect Effects 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 13
- 230000008878 coupling Effects 0.000 abstract description 8
- 238000010168 coupling process Methods 0.000 abstract description 8
- 238000005859 coupling reaction Methods 0.000 abstract description 8
- 239000002699 waste material Substances 0.000 description 44
- 239000012295 chemical reaction liquid Substances 0.000 description 6
- 239000012535 impurity Substances 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 239000003814 drug Substances 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 241000282414 Homo sapiens Species 0.000 description 2
- 230000003139 buffering effect Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 208000032376 Lung infection Diseases 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 208000004756 Respiratory Insufficiency Diseases 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 201000004193 respiratory failure Diseases 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F7/00—Aeration of stretches of water
Abstract
The invention discloses a synthetic ammonia industry pollutant processing device, relates to the technical field of pollutant processing devices, and aims to solve the problems that an existing pollutant processing device is poor in processing effect and easy to cause secondary pollution. The top of synthetic ammonia reservoir is provided with the transfer line, the inside of transfer line is provided with the cartridge filter, one side of synthetic ammonia reservoir is provided with the supporting seat, the top of supporting seat is provided with the reacting chamber, one side of reacting chamber top is provided with the feed liquor pipe, one side of feed liquor pipe is provided with the liquid feeding pipe, one side of liquid feeding pipe is provided with exhaust outlet, the one end of transfer line extends to the inside of feed liquor pipe, one side of reacting chamber is provided with the motor room, the internally mounted of motor room has the motor, be provided with the shaft coupling on the output of motor, the motor passes through shaft coupling and (mixing) shaft fixed connection, be provided with the stirring leaf on the outer wall of (mixing) shaft, and the stirring leaf is.
Description
Technical Field
The invention relates to the technical field of pollutant treatment devices, in particular to a device for treating pollutants in synthetic ammonia industry.
Background
Along with the rapid development of economy in China, the living standard of people is remarkably improved, and simultaneously, a large amount of pollutants such as water pollution are discharged to the nature, so that most of surface water and underground water in China are polluted, and the content of ammonia nitrogen in some water source water exceeds the national standard. As the ammonia nitrogen has great potential harm to human beings, the highest limit standard of the content of the ammonia nitrogen in drinking water is determined in many countries in the world. The development of synthetic ammonia is increased along with the rapid development of industry, but the problems are also followed, the synthetic ammonia wastewater is mainly characterized by high-nitrogen ammonia, and if the synthetic ammonia wastewater is directly discharged into water without treatment, eutrophication of the water body is caused, and the natural state of the water body is damaged. Ammonia is one of typical toxic and harmful industrial gaseous pollutants, and a large amount of ammonia-containing industrial tail gas is directly discharged into the atmosphere, so that the loss of synthetic ammonia products is caused, and the living environment of people is deteriorated. Ammonia is oxidized in the atmosphere to generate NOx, acid rain is formed, and the NOx is further oxidized into nitrate and enters a water circulation system to pollute underground water. In addition, ammonia can be harmful to human health, and serious patients can cause lung infection and respiratory failure to die.
The existing pollutant treatment device has poor treatment effect and is easy to cause secondary pollution; therefore, the existing requirement is not met, and a pollutant treatment device for the synthetic ammonia industry is provided for the requirement.
Disclosure of Invention
The invention aims to provide a synthetic ammonia industrial pollutant treatment device, which solves the problems that the existing pollutant treatment device in the background art has poor treatment effect and is easy to cause secondary pollution.
In order to achieve the purpose, the invention provides the following technical scheme: a synthetic ammonia industrial pollutant processing device comprises a synthetic ammonia liquid storage tank, wherein a liquid conveying pipe is arranged above the synthetic ammonia liquid storage tank, a filter cylinder is arranged inside the liquid conveying pipe, a supporting seat is arranged on one side of the synthetic ammonia liquid storage tank, a reaction chamber is arranged above the supporting seat, a liquid inlet pipe is arranged on one side above the reaction chamber, a liquid adding pipe is arranged on one side of the liquid inlet pipe, a waste gas outlet is arranged on one side of the liquid adding pipe, one end of the liquid conveying pipe extends into the liquid inlet pipe, a motor chamber is arranged on one side of the reaction chamber, a motor is arranged inside the motor chamber, a shaft coupling is arranged on the output end of the motor, the motor is fixedly connected with a stirring shaft through the shaft coupling, stirring blades are arranged on the outer wall of the stirring shaft and are arranged in twelve numbers, a switch is arranged, one side of reacting chamber below is provided with the drain pipe, the below of drain pipe is provided with output pipeline, output pipeline's inside is provided with the drawing liquid pump, output pipeline's one end extends to the inside of gas-liquid filter room, the inside of gas-liquid filter room is provided with the filter chamber, one side of gas-liquid filter room is provided with the air pump, the air pump passes through gas-supply pipe and gas-liquid filter room fixed connection, the opposite side of gas-liquid filter room is provided with deposits the recovery pond, and deposits the recovery pond and pass through fluid-discharge tube and gas-liquid filter room fixed connection, the inside of cartridge filter is provided with coarse strainer layer, one side of coarse strainer layer is provided with the fine filter layer, the both sides of cartridge filter all are provided with the.
Preferably, one side of the filter cylinder is provided with a liquid flow meter.
Preferably, the reaction chamber is internally provided with a heating pipe.
Preferably, the inside of filter chamber is provided with the baffle, and the baffle is provided with two.
preferably, a stop valve is arranged inside the liquid outlet pipe.
Preferably, one side of the gas transmission pipe is provided with an aeration pipe.
Preferably, one side of the fine filter screen layer is provided with an outlet orifice plate.
Preferably, the outlet pore plate is provided with six water caps.
Preferably, a spoiler is arranged between the two partition plates.
Preferably, through holes are formed in the two partition plates.
Compared with the prior art, the invention has the beneficial effects that:
1. According to the invention, through the arrangement of the reaction chamber, the reaction liquid medicine is added into the liquid adding pipe, the PH value of the waste liquid can be adjusted, then the motor is started, the output end of the motor drives the stirring shaft to rotate through the coupler, so that the stirring blade starts to stir the liquid in the reaction chamber, through the arrangement of the heating pipe, the heating pipe can not only accelerate the reaction of the waste liquid and the reaction liquid medicine, but also sterilize the waste liquid, the waste gas outlet can play a role in ventilation, and the waste gas is discharged into the exhaust pipeline.
2. Through the setting of cartridge filter, the inside of cartridge filter is provided with the coarse filtration stratum reticulare, can carry out a primary filter to solid impurity in waste liquid and the waste gas, later get into fine filter screen layer and carry out the secondary filter, a good filtering action has been played, through the setting of export orifice plate, not only can filter the filter material, can play the effect of a buffering to rivers in addition, reduce the velocity of flow of rivers, through the setting of water cap, impurity can effectually be washed out, guarantee quality of water normal operating, the filterable effect has been strengthened.
3. Through the setting of gas-liquid filter chamber, after output pipeline is with waste liquid defeated inlet gas liquid filter chamber, at first get into the filter chamber and filter, the inside of gas-liquid filter chamber is provided with two baffles, two baffles divide into the filter chamber threely, the waste liquid loops through three filter chamber and filters, the inside of two baffles all is provided with a plurality of through-hole, the through-hole can weaken the flow velocity of liquid, make the filtration that the waste liquid can be better, through the setting of spoiler, the spoiler sets up between two baffles, can increase the contact of waste liquid and filter chamber and baffle.
4. Through the setting of air pump and aeration pipe, start the air pump, the air pump passes through the gas-supply pipe and in with air compression suction aeration pipe, overflows with bubble form dispersion again, with oxygen fusion in liquid, the aeration pipe can improve the oxygen content of waste liquid, the filtration of waste liquid with higher speed.
5. Through the setting of deposiing the recovery pond, get into through the fluid-discharge tube after gas-liquid filter room filters and adsorbs the waste liquid and deposit the recovery pond and carry out recycle, make the waste liquid that purifies become but recycle's reuse water, the rethread delivery pipe discharges away, has improved the reuse rate of water resource.
6. Through the setting of fluidflowmeter, can record how much of feed liquor volume to the flow of control feed liquor, through the setting of stop valve, the stop valve can control the flow and static of liquid, and can play sealed effect when closing.
Drawings
FIG. 1 is a schematic view of the overall structure of the present invention;
FIG. 2 is a schematic view of the internal structure of the reaction chamber according to the present invention;
FIG. 3 is a schematic view of the internal structure of the filter cartridge of the present invention;
FIG. 4 is a schematic view of the gas-liquid filtering chamber structure of the present invention;
FIG. 5 is a schematic diagram of a side view of the separator of the present invention;
In the figure: 1. a synthetic ammonia reservoir; 2. a transfusion tube; 3. a filter cartridge; 301. a coarse filter screen layer; 302. a fine screen layer; 303. an outlet orifice plate; 304. a water cap; 305. a leakage-proof ring; 306. a joint; 4. a liquid flow meter; 5. a liquid inlet pipe; 6. a liquid feeding pipe; 7. an exhaust gas outlet; 8. a reaction chamber; 9. a motor chamber; 10. a switch; 11. a supporting seat; 12. a liquid outlet pipe; 13. an output pipe; 14. a liquid pump; 15. an air pump; 16. a gas delivery pipe; 17. a gas-liquid filtering chamber; 18. a liquid discharge pipe; 19. a sedimentation recovery tank; 20. a motor; 21. a coupling; 22. a stirring shaft; 23. stirring blades; 24. heating a tube; 25. a stop valve; 26. a partition plate; 27. a filter chamber; 28. a spoiler; 29. an aeration pipe; 30. and a through hole.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments.
Referring to fig. 1-5, an embodiment of the present invention is shown: a synthetic ammonia industrial pollutant processing device comprises a synthetic ammonia liquid storage tank 1, a liquid conveying pipe 2 is arranged above the synthetic ammonia liquid storage tank 1, a filter cartridge 3 is arranged inside the liquid conveying pipe 2, the filter cartridge 3 has a good primary filtering effect on waste liquid, a supporting seat 11 is arranged on one side of the synthetic ammonia liquid storage tank 1, the supporting seat 11 has the effect of supporting and stabilizing a reaction chamber 8, a reaction chamber 8 is arranged above the supporting seat 11, a liquid inlet pipe 5 is arranged on one side above the reaction chamber 8, a liquid adding pipe 6 is arranged on one side of the liquid inlet pipe 5, the liquid adding pipe 6 is used for adding reaction liquid medicine to adjust the PH value of the neutralized waste liquid, a waste gas outlet 7 is arranged on one side of the liquid adding pipe 6, the waste gas outlet 7 can play a ventilating effect, waste gas is discharged into an exhaust pipeline, one end of the liquid conveying pipe 2 extends to the inside of the liquid inlet pipe 5, a, a motor 20 is arranged in the motor chamber 9, a shaft coupling 21 is arranged at the output end of the motor 20, the motor 20 is fixedly connected with a stirring shaft 22 through the shaft coupling 21, stirring blades 23 are arranged on the outer wall of the stirring shaft 22, twelve stirring blades 23 are arranged on the outer wall of the stirring shaft 22, the output end of the motor 20 drives the stirring shaft 22 to rotate through the shaft coupling 21, so that the stirring blades 23 start to stir liquid in the reaction chamber 8, a switch 10 is arranged below the reaction chamber 8, a liquid outlet pipe 12 is arranged on one side below the reaction chamber 8, an output pipeline 13 is arranged below the liquid outlet pipe 12, a liquid pump 14 is arranged in the output pipeline 13, one end of the output pipeline 13 extends into the gas-liquid filtering chamber 17, the liquid pump 14 pumps waste liquid into the gas-liquid reaction chamber 8 through the output pipeline 13, a filtering chamber 27 is arranged in the gas-liquid filtering chamber 17, and an, the air pump 15 is fixedly connected with the gas-liquid filtering chamber 17 through an air pipe 16, the other side of the gas-liquid filtering chamber 17 is provided with a precipitation recovery tank 19, the precipitation recovery tank 19 is fixedly connected with the gas-liquid filtering chamber 17 through a liquid discharge pipe 18, the waste liquid is filtered and adsorbed by the gas-liquid filtering chamber 17 and then enters the precipitation recovery tank 19 through the liquid discharge pipe 18 for recycling, so that the purified waste liquid is changed into recyclable reuse water and then is discharged through a discharge pipe, the recycling rate of water resources is improved, a coarse filter screen layer 301 is arranged inside the filtering cylinder 3 and can carry out primary filtering on solid impurities in the waste liquid and the waste gas, one side of the coarse filter screen layer 301 is provided with a fine filter screen layer 302 which can carry out secondary intermediate filtering on the waste liquid, joints 306 are arranged on both sides of the filtering cylinder 3, the liquid pipe 2 is fixedly connected with the filtering cylinder 3 through, the leakage prevention ring 305 plays a role in preventing the waste liquid from leaking.
Further, one side of cartridge filter 3 is provided with fluidflowmeter 4, and fluidflowmeter 4 can record how much of feed liquor volume to the flow of control feed liquor.
Further, the heating pipe 24 is installed inside the reaction chamber 8, and the heating pipe 24 not only can accelerate the reaction between the waste liquid and the reaction liquid, but also can sterilize the waste liquid.
Further, the inside of filter chamber 27 is provided with baffle 26, and baffle 26 is provided with two, and two baffles 26 divide into three with filter chamber 27, and the waste liquid loops through three filter chamber 27 and filters and purifies.
Further, the inside of the liquid outlet pipe 12 is provided with a stop valve 25, and the stop valve 25 can control the flow and the standstill of the liquid and can play a role of sealing when being closed.
Further, an aeration pipe 29 is arranged on one side of the gas transmission pipe 16, the air pump 15 compresses and pumps air into the aeration pipe 29 through the gas transmission pipe 16, and then the air is dispersed and escaped in a bubble form to fuse oxygen into liquid, and the aeration pipe 29 can improve the oxygen content of waste liquid and accelerate the filtration of the waste liquid.
Further, one side of fine filter screen layer 302 is provided with export orifice plate 303, and export orifice plate 303 not only can filter the filter material, can play the effect of a buffering to rivers moreover, reduces the velocity of flow of rivers.
Further, outlet hole plate 303 is last to be provided with water cap 304, and water cap 304 is provided with six, and water cap 304 can effectual washout impurity, guarantees quality of water yield normal operating, has strengthened filterable effect.
Further, a baffle plate 28 is disposed between the two partition plates 26, and the baffle plate 28 is disposed between the two partition plates 26, so as to increase the contact between the waste liquid and the filter chamber 27 and the partition plates 26.
Further, the through holes 30 are formed in the two partition plates 26, and the flowing speed of liquid can be weakened through the through holes 30, so that waste liquid can be better filtered.
the working principle is as follows: when in use, the waste liquid in the synthetic ammonia liquid storage tank 1 is conveyed to the inside of the reaction chamber 8 through the liquid conveying pipe 2, the filter cylinder 3 is arranged in the liquid conveying pipe 2, the coarse filter screen layer 301 is arranged in the filter cylinder 3, solid impurities in the waste liquid and the waste gas can be primarily filtered, and then the waste liquid and the waste gas enter the fine filter screen layer 302 for secondary filtering, so that a good filtering effect is achieved, the filter material can be filtered through the outlet pore plate 303, the water flow can be buffered, the flow rate of the water flow is reduced, the impurities can be effectively washed out through the arrangement of the water cap 304, the normal operation of the water quality and the water quantity is ensured, the filtering effect is enhanced, the liquid flow meter 4 is arranged on one side of the filter cylinder 3, the quantity of the liquid inlet can be measured through the arrangement of the liquid flow meter 4, and the flow of the liquid inlet is controlled, then adding reaction liquid medicine from the liquid adding pipe 6, adjusting the PH value of the waste liquid, then pressing the switch 10, starting the motor 20, driving the stirring shaft 22 to rotate by the output end of the motor 20 through the coupler 21, so that the stirring blade 23 starts to stir the liquid in the reaction chamber 8, through the arrangement of the heating pipe 24, the heating pipe 24 can not only accelerate the reaction of the waste liquid and the reaction liquid medicine, but also sterilize the waste liquid, the waste gas outlet 7 can play a role of ventilation, and discharge the waste gas into the exhaust pipe, after the stirring is finished, opening the stop valve 25, allowing the waste liquid to enter the output pipe 13 from the liquid outlet pipe 12, through the arrangement of the stop valve 25, the stop valve 25 can control the flow and the rest of the liquid, and can play a role of sealing when being closed, the liquid pump 14 is arranged in the transmission pipe, the liquid pump 14 pumps the waste liquid into the gas-liquid reaction, through the arrangement of the gas-liquid filter chamber 17, after the output pipeline 13 conveys the waste liquid into the gas-liquid filter chamber 17, the waste liquid firstly enters the filter chamber 27 for filtering, two partition plates 26 are arranged inside the gas-liquid filter chamber 17, the filter chamber 27 is divided into three by the two partition plates 26, the waste liquid is filtered by sequentially passing through the three filter chambers 27, a plurality of through holes 30 are arranged inside the two partition plates 26, the through holes 30 can weaken the flowing speed of the liquid, so that the waste liquid can be better filtered, through the arrangement of the spoiler 28, the spoiler 28 is arranged between the two partition plates 26, the contact between the waste liquid and the filter chamber 27 and the partition plates 26 can be increased, the aeration pipe 29 is arranged at the bottom of the gas-liquid filter chamber 17, through the cooperation of the air pump 15 and the aeration pipe 29, the air pump 15 compresses and sucks air into the aeration pipe 29 through the air conveying pipe 16, aeration pipe 29 can improve the oxygen content of waste liquid, accelerates the filtration of waste liquid, filters and adsorbs the waste liquid through gas-liquid filter chamber 17, gets into sediment recovery pond 19 through fluid-discharge tube 18 at last and carries out recycle, makes the waste liquid that purifies become but recycle's reuse water, and the rethread delivery pipe discharges away, has improved the reuse rate of water resource.
It will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, and that the present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Claims (10)
1. a synthetic ammonia industry pollutant processing apparatus, includes synthetic ammonia reservoir (1), its characterized in that: the device is characterized in that a transfusion tube (2) is arranged above the synthetic ammonia liquid storage tank (1), a filter cartridge (3) is arranged inside the transfusion tube (2), a supporting seat (11) is arranged on one side of the synthetic ammonia liquid storage tank (1), a reaction chamber (8) is arranged above the supporting seat (11), a liquid inlet tube (5) is arranged on one side above the reaction chamber (8), a liquid adding tube (6) is arranged on one side of the liquid inlet tube (5), a waste gas outlet (7) is arranged on one side of the liquid adding tube (6), one end of the transfusion tube (2) extends into the liquid inlet tube (5), a motor chamber (9) is arranged on one side of the reaction chamber (8), a motor (20) is arranged inside the motor chamber (9), a coupler (21) is arranged on the output end of the motor (20), and the motor (20) is fixedly connected with a stirring shaft (22) through the coupler (21), stirring blades (23) are arranged on the outer wall of the stirring shaft (22), twelve stirring blades (23) are arranged, a switch (10) is arranged below the reaction chamber (8), a liquid outlet pipe (12) is arranged on one side below the reaction chamber (8), an output pipeline (13) is arranged below the liquid outlet pipe (12), a liquid pump (14) is arranged inside the output pipeline (13), one end of the output pipeline (13) extends into the gas-liquid filtering chamber (17), a filtering chamber (27) is arranged inside the gas-liquid filtering chamber (17), an air pump (15) is arranged on one side of the gas-liquid filtering chamber (17), the air pump (15) is fixedly connected with the gas-liquid filtering chamber (17) through an air pipe (16), a precipitation recovery tank (19) is arranged on the other side of the gas-liquid filtering chamber (17), and the precipitation recovery tank (19) is fixedly connected with the gas-liquid filtering chamber (17) through a liquid discharge pipe (18), the inside of cartridge filter (3) is provided with coarse strainer layer (301), one side of coarse strainer layer (301) is provided with fine strainer layer (302), the both sides of cartridge filter (3) all are provided with joint (306), be provided with leak protection circle (305) on the outer wall of joint (306).
2. the pollutant treatment device in the synthetic ammonia industry according to claim 1, characterized in that: and a liquid flowmeter (4) is arranged on one side of the filter cylinder (3).
3. The pollutant treatment device in the synthetic ammonia industry according to claim 1, characterized in that: and a heating pipe (24) is arranged in the reaction chamber (8).
4. the pollutant treatment device in the synthetic ammonia industry according to claim 1, characterized in that: the filter cavity (27) is internally provided with two partition plates (26), and the number of the partition plates (26) is two.
5. The pollutant treatment device in the synthetic ammonia industry according to claim 1, characterized in that: a stop valve (25) is arranged inside the liquid outlet pipe (12).
6. The pollutant treatment device in the synthetic ammonia industry according to claim 1, characterized in that: an aeration pipe (29) is arranged on one side of the gas transmission pipe (16).
7. The pollutant treatment device in the synthetic ammonia industry according to claim 1, characterized in that: an outlet orifice plate (303) is arranged on one side of the fine filter screen layer (302).
8. The pollutant treating device for synthetic ammonia industry according to claim 7, characterized in that: the outlet pore plate (303) is provided with six water caps (304), and the number of the water caps (304) is six.
9. The pollutant treatment device in the synthetic ammonia industry according to claim 4, characterized in that: a flow blocking plate (28) is arranged between the two partition plates (26).
10. The pollutant treatment device in the synthetic ammonia industry according to claim 4, characterized in that: through holes (30) are formed in the two partition plates (26).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910854310.2A CN110550803A (en) | 2019-09-10 | 2019-09-10 | Synthetic ammonia industry pollutant processing apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910854310.2A CN110550803A (en) | 2019-09-10 | 2019-09-10 | Synthetic ammonia industry pollutant processing apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110550803A true CN110550803A (en) | 2019-12-10 |
Family
ID=68739737
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910854310.2A Pending CN110550803A (en) | 2019-09-10 | 2019-09-10 | Synthetic ammonia industry pollutant processing apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110550803A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111762987A (en) * | 2020-07-13 | 2020-10-13 | 甘肃农业大学 | Fermentation device for livestock husbandry excrement treatment |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN208414134U (en) * | 2018-03-21 | 2019-01-22 | 广东玖翼化工有限公司 | A kind of liquid waste treating apparatus |
-
2019
- 2019-09-10 CN CN201910854310.2A patent/CN110550803A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN208414134U (en) * | 2018-03-21 | 2019-01-22 | 广东玖翼化工有限公司 | A kind of liquid waste treating apparatus |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111762987A (en) * | 2020-07-13 | 2020-10-13 | 甘肃农业大学 | Fermentation device for livestock husbandry excrement treatment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205398399U (en) | Rural domestic sewage treatment equipment | |
| CN111068450A (en) | Flue gas dust removal and purification device | |
| CN110550803A (en) | Synthetic ammonia industry pollutant processing apparatus | |
| CN204417254U (en) | Metal wire-drawing waste liquid oil-water separation purification device | |
| CN110282775A (en) | Integrated sewage treating apparatus | |
| CN211078671U (en) | Filter equipment for municipal administration sewage treatment | |
| CN104941351A (en) | Harmless high-efficiency treatment device for industrial chimney | |
| CN211471158U (en) | Filter equipment for sewage treatment | |
| CN209039217U (en) | A kind of chemical industry purifying sewage quickly device | |
| CN207828025U (en) | A kind of chemical engineering sewage pond decontamination apparatus | |
| CN208218511U (en) | The processing unit of high-concentration sewage | |
| CN207243617U (en) | Desulfurizing waste water processing device | |
| CN206927727U (en) | A kind of sewage-treatment plant | |
| CN210656481U (en) | High-concentration ammonia nitride processing device | |
| CN212713155U (en) | Membrane method ammonia nitrogen removal device | |
| CN211471139U (en) | Biological sewage treatment device | |
| CN216987224U (en) | Wastewater treatment equipment with quick cooling function | |
| CN210825743U (en) | Filter equipment for sewage treatment | |
| CN216837413U (en) | Medical purification is preprocessing device for water system | |
| CN213388120U (en) | Automatic integrated water purification device for coal mine wastewater | |
| CN220766624U (en) | Natural water treatment device based on ceramic flat membrane | |
| CN215756846U (en) | Organic wastewater treatment equipment for aquaculture water | |
| CN219689469U (en) | Sewage treatment and recycling device | |
| CN216737886U (en) | Oxidation catalytic unit for environmental protection sewage treatment | |
| CN219603293U (en) | Engineering sewage treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20191210 |