TWM550298U - Ammonia removing apparatus and system for low concentration ammonia water and ammonia water producing system thereof - Google Patents

Abstract

An ammonia removing apparatus and system for low concentration ammonia water and an ammonia water producing system thereof are disclosed. The ammonia removing apparatus for low concentration ammonia water of the present application comprises an inner cylinder, an outer cylinder, a pressurizing channel and a heat exchanger, wherein a spiral channel is disposed between the inner cylinder and the outer cylinder. The low concentration ammonia water at the bottom of the outer cylinder is pressurized by the pressurizing channel and sprayed by a nozzle to form a plurality of droplets. A portion of ammonia and water evaporates from the droplets and forms ammonia gas and steam in an evaporation region of the inner cylinder. The droplets, ammonia gas and steam are separated in the spiral channel to obtain ammonia water of lower concentration, that the ammonia is removed from the low concentration ammonia water effectively.

Description

Low concentration ammonia deamination device, low concentration ammonia deamination system and ammonia production system

This creation is about a low concentration ammonia deamination unit, a low concentration ammonia deamination system and an ammonia production system.

Ammonia is a commonly used substance in the industry, but it often produces ammonia-containing wastewater after use. Because ammonia has a pungent odor, and ammonia gas generated by ammonia or ammonia volatilization is an important source of environmental pollution. Therefore, ammonia-containing wastewater is usually denitrified before it can be discharged or recycled.

Generally, there are two types of deamination treatment of waste ammonia water, one of which is to blow ammonia in waste ammonia water into ammonia gas by air stripping; the other is to distill ammonia gas by heating and evaporation. However, when the ammonia concentration is low, both the stripping method and the heating evaporation method will face problems of high energy consumption and low efficiency. The following are discussed separately.

When using the stripping method, a large or large number of blowers are required to press a large amount of air into the water body, which consumes a large amount of electricity and generates high decibel noise. It takes time for the ammonia in the aqueous phase to diffuse to the gas-liquid interface. Assuming that the distance between the bubble and the bubble is 0.1-1 cm, the diffusion distance of ammonia is 0.05-0.5 cm, and the mass transfer distance limits the efficiency of the stripping method. Therefore, the apparatus using the stripping method is bulky, and it is difficult to reduce the concentration of a large amount of ammonia water to a standard allowed by the regulations in a short time.

When the heating evaporation method is used, heating causes ammonia to volatilize into ammonia gas, and a large amount of moisture is generated, so that a large amount of heat energy is lost. Further, when the heating evaporation method is used, the water film thickness is about 0.1 to several centimeters, so that it takes longer for ammonia to diffuse from the water body to the gas-liquid interface.

Therefore, how to provide a solution for high-efficiency deamination of low-concentration ammonia water is an urgent problem to be solved in the industry.

One of the purposes of this creation is to provide a low concentration ammonia deamination device, especially a low concentration ammonia deamination device, a low concentration ammonia deamination system and an ammonia production system.

Another object of the present invention is to provide a low-concentration ammonia deamination device, which can reduce the mass transfer resistance by atomization, and can improve the deamination efficiency.

Another object of the present invention is to provide a low-concentration ammonia deamination device for increasing the ammonia gas content in the vapor at a low pressure operation, thereby improving the deamination efficiency.

Another object of the present invention is to provide a low-concentration ammonia deamination device which can provide heat required for ammonia volatilization by using a heat pump, and can reduce the energy loss required for deamination.

Another object of the present invention is to provide a low-concentration ammonia deamination system, which can enhance the deamination effect and further reduce the ammonia content in the recovered water by the serial use of the deamination device.

Another object of the present invention is to provide a low-concentration ammonia water production system, which can utilize the deamination system of the present invention and the condensate tank design to make the ammonia gas extracted from the waste ammonia water into a higher concentration of available ammonia water.

In order to achieve the above object, the present invention provides a low-concentration ammonia deamination device comprising: an inner cylinder, an internal space forming an evaporation zone, and an atomizing spray disposed on the upper portion of the evaporation zone The bottom of the inner tube is provided with a line opening along the tangential direction of the side wall; an outer tube is disposed around the inner tube, and an accommodating area is formed at the bottom of the outer tube for accommodating a low concentration ammonia water, and the accommodating area is provided with a line a water pipe and a feeding pipe, a spiral partition is arranged between the outer cylinder and the side wall of the inner cylinder to form a spiral passage, and an exhaust pipe is arranged at a top end of the spiral passage; a pressurized pipeline connects the receiving area and atomizes a nozzle, the pressure pipeline is provided with a pressure pump for extracting low concentration ammonia water and pressing, and then ejecting a plurality of droplets by the atomizing nozzle; and a heat exchanger is disposed on the pressure pipeline Heating a low concentration of ammonia water; wherein, part of the ammonia in the plurality of droplets in the evaporation zone evaporates with part of the water to form ammonia gas and water vapor, and the droplets, ammonia gas and water gas enter the spiral channel through the tangential opening and along the spiral The channel spirals upward, and a plurality of droplets collide with each other to condense and flow into the accommodating area from the lower opening of one of the spiral passages, and the ammonia gas and the water gas are discharged from the exhaust pipe.

In one embodiment of the present invention, the operating pressure of the inner and outer cylinders is less than 250 Torr.

In an embodiment of the present invention, wherein the diameter of the droplets is less than 1000 μm.

In an embodiment of the present invention, the heat exchanger is a heat release end of a heat pump.

In one embodiment of the present invention, wherein the operating temperature of the heat exchanger is below 65 °C.

In one embodiment of the present invention, the concentration of the low concentration ammonia water is less than 0.8% by weight.

The present invention also provides a low-concentration ammonia deamination system comprising: a plurality of low-concentration ammonia deamination devices as described in claim 1 of the patent application scope, and a plurality of low-concentration ammonia deamination devices comprising one of sequential series connection a first deamination device, a second deamination device to an Nth deamination device; Wherein, the outlet pipes of the respective deamination devices are respectively connected to the feed pipes of the latter deamination device, the feed pipes of the first deamination device are used to introduce low concentration ammonia water, and the outlet pipes of the Nth deamination device are used to discharge a recovered water. .

In an embodiment of the present invention, a water outlet pipe is connected to the outlet pipe of the Nth deamination device, wherein the water outlet pipe sequentially passes through the N-1 deamination device to the receiving portion of the first deamination device. .

In an embodiment of the present invention, a pumping pump is further included, which is disposed at the end of the water outlet pipe for extracting recycled water.

The present invention also provides an ammonia water production system comprising: a low concentration ammonia deamination system as described in claim 6 of the patent application, wherein the exhaust pipes of each deamination device are respectively connected to the evaporation zone of the previous deamination device The upper part of the condensing tank is provided with a condenser in the middle of the condensing tank, a second accommodating area is formed at the bottom, and a second exhaust pipe is arranged at the top, and the exhaust pipe of the first deaminating device is connected to the lower part of the condenser The condenser condenses the ammonia gas and the water gas discharged from the exhaust pipe to form a second low concentration ammonia water, the second low concentration ammonia water condenses and is accommodated in the second accommodating area, and the second accommodating area is provided with a first a second outlet pipe, a cold second exhaust pipe for discharging an ammonia gas; a pumping mixing unit connected to the second exhaust pipe for extracting ammonia gas and dissolving ammonia gas in water to form an ammonia water; and an ammonia The water tank is connected to an air suction mixing unit for accommodating ammonia water.

In an embodiment of the present invention, wherein the air extraction mixing unit is a venturi tube, the ammonia water production system further includes a circulation pipeline connecting the bottom of the ammonia water tank and the venturi tube, and the circulation pipeline is provided with a second pressure protection Pu, used to extract ammonia from the ammonia tank and pressurize it through the venturi to extract ammonia and dissolve the ammonia in the ammonia water.

In an embodiment of the present invention, wherein the second outlet pipe is connected to the first deamination device Feed tube.

10‧‧‧Low concentration ammonia deamination unit

101‧‧‧ Feeding tube

103‧‧‧Outlet pipe

105‧‧‧Exhaust pipe

12‧‧‧Deamination tank

120‧‧‧Outer tube

121‧‧‧ bottom

123‧‧‧ spiral partition

125‧‧‧Spiral channel

14‧‧‧Inner tube

140‧‧‧Evaporation zone

141‧‧‧ atomizing nozzle

143‧‧ tangential opening

16‧‧‧Pressure pipe

161‧‧‧Pressure pump

163‧‧‧ heat exchanger

18‧‧‧Low concentration ammonia

181‧‧‧

19‧‧‧ heat pump

20‧‧‧Low concentration ammonia deamination system

21‧‧‧First deamination unit

23‧‧‧Second deamination unit

25‧‧‧Water outlet

27‧‧‧ pumping pump

29‧‧‧Nth deamination unit

30‧‧‧Ammonia production system

31‧‧‧Second low concentration ammonia

32‧‧‧Condensation tank

321‧‧‧Condenser

323‧‧‧Second outlet

325‧‧‧Second exhaust pipe

327‧‧‧ bottom

33‧‧‧Ammonia

34‧‧‧Exhaust mixing unit

341‧‧‧ Venturi tube

36‧‧‧Ammonia sink

38‧‧‧Circulation line

381‧‧‧Second pressure pump

Fig. 1 is a schematic cross-sectional view showing an embodiment of a low-concentration ammonia deamination apparatus.

Fig. 2 is a schematic view showing an embodiment of a low-concentration ammonia deamination system.

Fig. 3 is a schematic view showing an embodiment of the present ammonia water production system.

Please refer to FIG. 1 , which is a schematic cross-sectional view of an embodiment of a low-concentration ammonia water deamination device. As shown, the present low concentration ammonia water removal unit 10 includes an inner cylinder 14, an outer cylinder 120, a pressurized line 16, and a heat exchanger 163. The inner space of the inner cylinder 14 forms an evaporation zone 140, and an atomizing nozzle 141 is disposed above the evaporation zone 140. The bottom of the inner cylinder 14 is provided with a line opening 143 along the tangential direction of the side wall. The outer cylinder 120 is disposed around the inner cylinder 14, and the bottom 121 of the outer cylinder 120 forms an accommodating area for accommodating a low concentration ammonia water 18. The receiving area is provided with an outlet pipe 103 and a feeding pipe 101. A spiral partition 123 is disposed between the outer cylinder 120 and the side wall of the inner cylinder 14 to form a spiral passage 125. An exhaust pipe 105 is disposed at the top end of the spiral passage 125, and a lower opening 127 is formed at the bottom end. The configuration of the outer cylinder 120 and the inner cylinder 14 forms the main body of the deaeration tank 12. The pressurizing line 16 is connected to the accommodating area of the outer tube 120 and the atomizing nozzle 141 of the inner tube 14. The pressurizing line 16 is provided with a pressurizing pump 161 for extracting the low concentration ammonia water 18 located in the accommodating area and performing After the pressurization, the atomizing nozzle 141 ejects to form a plurality of droplets 181. The heat exchanger 163 is disposed on the pressurizing line 16 for heating the low concentration ammonia water 18.

After the low concentration ammonia water 18 is ejected by the atomizing nozzle spray 141, a mist 181 is formed in the evaporation zone 140, and part of the ammonia and part of the water in the mist 181 evaporate to form ammonia gas and water vapor, and the evaporation station The heat required is provided by heat exchanger 163. Since the diameter of the droplet 181 is small and has a relatively large surface area, in addition to shortening the diffusion distance of ammonia in the liquid phase and reducing the mass transfer resistance, and having a large surface area, the ammonia can be evaporated by the gas-liquid interface. Ammonia.

In the evaporation zone 140, the mist 181, the ammonia gas and the moisture gas form a gas-liquid mixture, and the kinetic energy provided when the atomizing nozzle 141 is ejected moves in the evaporation zone 140. After passing through the tangential opening 143, the gas-liquid mixture will spiral up along the spiral passage 125. In the spiral passage 125, the droplet 181 will collide and adhere to the inner side wall of the outer cylinder 120 due to the action of centrifugal force and surface tension, forming a state of gas-liquid separation, and the ammonia gas and the water vapor can be discharged from the exhaust pipe 105. . When the droplet 181 adhered to the inner side wall of the outer cylinder 120 is subjected to the collision of the subsequent droplet 181, due to the surface tension, it will continuously merge and agglomerate, and finally a sufficiently large droplet is formed, which is attracted by gravity and slides along the spiral passage. Finally, the lower opening 127 flows into the accommodating area and is introduced into the low-concentration ammonia water 18.

By using the low concentration ammonia deamination device 10 of the present invention, the diffusion resistance of the mass transfer resistance and the ammonia in the liquid phase can be reduced by atomization, and the area of the gas-liquid interface can be increased, thereby improving the efficiency of deamination.

In one embodiment of the present invention, the operating pressure of the inner and outer cylinders 14 and 120 is less than 250 torr. In a low pressure environment, the ratio of the ammonia gas phase to the water vapor will increase, so reducing the operating pressure of the inner cylinder 14 and the outer cylinder 120 can increase the concentration of ammonia in the gas phase, and can also increase the low concentration ammonia deamination apparatus 10 Deamination efficiency.

In one embodiment of the present creation, the operating temperature of heat exchanger 163 is below 65 °C. When the operating pressure of the deaeration tank 12 is lowered, the internal equilibrium temperature is also lowered. For example, when a low concentration ammonia water having a weight percentage of 0.1% is treated under normal pressure, the equilibrium temperature is 99 ° C; when the operating pressure is lowered to 60 Torr, the equilibrium temperature is lowered to 36 ° C. Therefore, use the low concentration of this creation The ammonia ammonia deamination device 10 has an equilibrium temperature of between 30 and 50 ° C when the operating pressure of the deamination tank 12 is less than 250 Torr. Therefore, the operating temperature of the heat exchanger 163 is lower than 65 ° C to provide sufficient temperature and amount of heat for the demineralization operation of the low-concentration ammonia deamination apparatus 10.

In one embodiment of the present creation, heat exchanger 163 is a heat release end of a heat pump 19. In general, when the operating temperature is high, an electric heater or other heating device is used as a heat source for the heat exchanger 163. However, the deaerator tank 12 of the present invention is operated at a low pressure, so that the operating temperature can be lowered to below 65 °C. While this range of operating temperatures, the heat of the heat exchanger 163 can be provided by the heat pump 19. Since the heat pump 19 generally has three times efficiency, the energy loss of the deamination operation can be further reduced.

In one embodiment of the present invention, the droplets 181 have a diameter of less than 1000 μm. By using the low-concentration ammonia deamination device 10 of the present invention, the low-concentration ammonia water 18 is pressurized by the pressurizing pump 161, and the design of the atomizing nozzle 141 can effectively improve the atomization effect. The diameter of the droplet 181 is increased. Small, the smaller the mass transfer resistance, the higher the evaporation efficiency of ammonia. In an embodiment of the present invention, the low-concentration ammonia water 18 can be pressurized in the pressurizing line to have a pressure difference of ³ kgw/cm ² from the inside of the inner cylinder 14, and the mist nozzle can be used in conjunction with the action of the atomizing nozzle 141. The diameter of 181 is reduced to less than 1000 μm, which greatly increases the evaporation efficiency of ammonia. Since the ammonia in the deaerator tank 12 of the present invention has a relatively high evaporation efficiency, it is not necessary to design a large volume of the evaporation zone 140, and the volume of the low-concentration ammonia deamination apparatus 10 can be relatively reduced.

In one embodiment of the present invention, the concentration of the low concentration ammonia water is less than 0.8% by weight. In another embodiment of the present invention, the outlet pipe 103 can be disposed at the upper edge of the accommodating area, and when the liquid level of the low-concentration ammonia water 18 reaches the upper edge of the accommodating area, the overflow can be discharged.

Please refer to FIG. 2, which is a schematic diagram of an embodiment of a low-concentration ammonia water deamination system. The low concentration ammonia deamination system 20 of the present invention comprises a plurality of low concentrations as shown in Figure 1 The ammonia water deamination device 10 and the low-concentration ammonia water deamination devices 10 are sequentially connected in series. It is assumed that a plurality of low-concentration ammonia deamination devices 10 include a first deamination device 21, a second deamination device 23, and an N-de ammonia removal device (see FIG. 3, 29). The outlet pipes 103 of the respective deamination devices 21, 23, 29 are respectively connected to the feed pipe 101 of the subsequent deamination devices 23, 29, and the feed pipe 101 of the first deamination device 21 is used to introduce the low concentration ammonia water 18, Nth The outlet pipe 103 of the deamination unit 29 is for discharging a recovered water. Among them, the more the deamination device is connected in series, the lower the concentration of ammonia contained in the recovered recovered water. According to the experimental results, the low-concentration ammonia deamination system 20 of the present invention can be seen that 4-6 low-concentration ammonia deamination devices are connected in series, and the ammonia content in the recovered water can be reduced to 5-30 ppm, which meets the regulatory allowable standard.

In the second figure, two low-concentration ammonia deamination devices are connected in series as an example. Those having ordinary knowledge in the technical field of the present invention can infer from the same principle to obtain a plurality of serially connected structures. As shown in the figure, the present embodiment has a first deamination device 21 and a second deamination device 23, wherein the outlet pipe 103 of the first deamination device 21 is connected to the feed pipe 101 of the second deamination device 23. Therefore, the low-concentration ammonia water 18 after the deamination operation by the first deamination device 21 can enter the second deamination device 23, thereby performing the next stage of deamination operation. When the system 20 has a plurality of deamination devices, a multi-stage deamination operation can be sequentially performed to gradually reduce the ammonia content in the low concentration ammonia water.

The ammonia gas and the water gas discharged from the exhaust pipe 105 of each of the deamination devices 21 and 23 may be collected separately or collectively, and then subjected to subsequent treatment. In an embodiment of the present invention, the exhaust pipe 105 of each deamination device (for example, the second deamination device 23) may be connected to the evaporation zone 140 of the previous deamination device (for example, the first deamination device 21). In the upper portion, the ratio of ammonia gas to water vapor in the evaporation zone 140 of the previous deamination unit is redistributed to increase the ammonia gas content produced by the previous deamination unit.

In one embodiment of the present invention, the low concentration ammonia deamination system 20 further includes a water outlet line 25 connected to the last deamination unit (e.g., the second deamination unit 23 or the Nth strip in Fig. 3). The water outlet pipe 103 of the ammonia device 29), and the water outlet pipe 25 is reversely passed through the accommodating zone of the preceding deamination device (for example, the first deamination device 21) and then discharged. Since each of the deaminating devices 21 and 23 respectively heats the low-concentration ammonia water 18, the low-concentration ammonia water 18 connected in series to the rear-end deamination device will have a higher temperature, and the water-removing pipe 25 will be used to reverse the recovered water. By passing through the respective deamination devices connected in series, the low-concentration ammonia water of each deamination device can be heated by the residual temperature of the recovered water to further reduce the loss of heat.

In one embodiment of the present invention, the low-concentration ammonia deamination system 20 further includes a pumping pump 27 disposed at the end of the water outlet line 25 for extracting recovered water and providing recovered water for storage through each deamination unit. The power of the district.

Please refer to FIG. 3 , which is a schematic diagram of an embodiment of the ammonia production system. As shown, the present ammonia production system 30 includes a low concentration ammonia deamination system 20, a condensate tank 32, a pumping mixing unit 34, and an ammonia tank 36 as described in FIG. Among them, the exhaust pipes 105 of the respective deamination devices 23 and 29 in the low-concentration ammonia deamination system 20 are respectively connected to the upper portions of the evaporation zones 140 of the previous deamination devices 21 and 23. With this configuration, the ammonia gas discharged from each of the deamination devices 23, 29 can be sent to the evaporation zone 140 of the previous deamination devices 21, 23 to produce a reverse concentration effect.

A condenser 321 is disposed in the middle of the condensing tank 32. The bottom portion 327 forms a second accommodating area, and the top portion is provided with a second exhaust pipe 325. The exhaust pipe 105 of the first deamination device 21 is connected to the lower side of the condenser 321, and the ammonia gas and the water gas discharged from the exhaust pipe 105 of the first deamination device 21 can be condensed by the condenser 321. Since the condensation conditions of the ammonia gas and the water gas are different, the condenser 321 will condense most of the water vapor with a small portion of the ammonia gas into the second low concentration ammonia water 31 and be accommodated in the second accommodating zone. The amount of ammonia in the remaining gas will be greatly increased, and in one embodiment of the present invention, it is about 35%. This high concentration ammonia gas can be discharged from the second exhaust pipe 325. In this creation In one embodiment, the condenser 321 can be cooled using ice water.

The air suction mixing unit 34 is connected to the second exhaust pipe 325 for extracting ammonia gas and dissolving the ammonia gas in the water to form the ammonia water 33. The ammonia water tank 36 is connected to the air suction mixing unit 34 for accommodating the ammonia water 33. Since the low-concentration ammonia deammification device and system of the present invention have a low operating pressure, it is necessary to extract a high concentration of ammonia gas by a suction device (for example, a vacuum pump), perform pressure balance, and then mix with water to dissolve ammonia. Ammonia is formed in the water. Aqueous percent concentration of 20-36% ammonia water can be obtained via a suitable design mixing circuit. This concentration of ammonia has been of economic value and can be processed by subsequent purification equipment to produce pure ammonia or electronic grade ammonia.

In one embodiment of the present invention, the air extraction mixing unit 34 is a venture-tube 341. The ammonia water production system 30 further includes a circulation line 38 connecting the bottom of the ammonia water tank 36 to the venturi 341 for circulation. A second pressurizing pump 381 is provided in the line 38 for extracting the ammonia water 33 in the ammonia tank 36 and pressurizing it through the venturi 341. The second exhaust pipe 325 is connected to the neck of the venturi 341, and the ammonia gas in the second exhaust pipe 325 is extracted by the negative pressure generated by the high flow rate of the ammonia water 33 at the neck of the venturi 341, and the ammonia gas is obtained. The mixture is mixed and dissolved in the ammonia water 33 to increase the concentration of the ammonia water 33.

In an embodiment of the present invention, the second outlet pipe 323 of the condensation tank 32 can be connected to the feed pipe 101 of the first deamination device 21, and the second low concentration ammonia water 31 produced can be introduced into the low concentration ammonia water for ammonia removal. System 20 performs a deamination operation.

The low-concentration ammonia deamination device and system of the present invention can perform high-efficiency and low-energy deamination operation for low-concentration ammonia water. According to calculations and experimental statistics, the operation cost per ton of low-concentration ammonia water to meet the emission standards (including electricity and personnel costs) is about NT$100 or RMB24, which is very economical and energy-saving. With the ammonia water production system of the present creation, in the process of deamination, the ammonia gas produced can be made into ammonia with economic value and can be returned. Recycling will further reduce the burden on the environment and compensate for the cost of deamination.

The above is only the embodiment of the present invention, and is not intended to limit the scope of the present invention, that is, the uniformity and modification of the shapes, structures, features, methods and spirits described in the scope of the patent application. , should be included in the scope of the patent application of this creation.

10‧‧‧Low concentration ammonia deamination unit

101‧‧‧ Feeding tube

103‧‧‧Outlet pipe

105‧‧‧Exhaust pipe

12‧‧‧Deamination tank

120‧‧‧Outer tube

121‧‧‧ bottom

123‧‧‧ spiral partition

125‧‧‧Spiral channel

14‧‧‧Inner tube

140‧‧‧Evaporation zone

141‧‧‧ atomizing nozzle

143‧‧ tangential opening

16‧‧‧Pressure pipe

161‧‧‧Pressure pump

163‧‧‧ heat exchanger

18‧‧‧Low concentration ammonia

181‧‧‧

19‧‧‧ heat pump

Claims (12)

A low-concentration ammonia water deamination device comprises: an inner cylinder, an inner space forming an evaporation zone, and an atomizing nozzle disposed on an upper portion of the evaporation zone, wherein the bottom of the inner cylinder is provided with a line opening along a tangential direction of the side wall; An outer cylinder is disposed around the inner cylinder, and an outer portion of the outer cylinder forms a receiving area for accommodating a low concentration ammonia water, wherein the accommodating area is provided with an outlet pipe and a feeding pipe, the outer cylinder and the inner tube A spiral partition is arranged between the side walls of the cylinder to form a spiral passage. The top end of the spiral passage is provided with an exhaust pipe; a pressurized pipeline connecting the receiving area and the atomizing nozzle, the pressurized pipeline is provided a pressure pump for extracting the low concentration ammonia water and pressurizing, and then spraying the atomization nozzle to form a plurality of droplets; and a heat exchanger disposed on the pressure pipeline for heating the low a concentration of ammonia water; wherein, in the evaporation zone, part of the ammonia and part of the water in the plurality of droplets evaporate to form ammonia gas and water vapor, and the mist, the ammonia gas and the water gas enter the spiral channel through the tangential opening And spiraling along the spiral channel, the plurality of Aggregated droplets collide with each other and by one of the spiral channel beneath the opening into the accommodation area, the ammonia gas with the water by the exhaust pipe. The low-concentration ammonia deamination apparatus according to claim 1, wherein the inner cylinder and the outer cylinder have an operating pressure of less than 250 Torr. A low-concentration ammonia deamination apparatus as described in claim 2, wherein the heat exchanger has an operating temperature of less than 65 °C. The low-concentration ammonia deamination device according to claim 3, wherein the heat exchanger is a heat release end of a heat pump. A low-concentration ammonia deamination device as described in claim 1, wherein the diameter of the droplet Less than 1000 μm. The low-concentration ammonia deamination apparatus according to claim 1, wherein the low-concentration ammonia water has a weight percentage concentration of less than 0.8%. A low-concentration ammonia deamination system comprising: a plurality of low-concentration ammonia deamination devices as described in claim 1 of the patent scope, the plurality of low-concentration ammonia deamination devices comprising one of the first An ammonia device, a second deamination device to an Nth deamination device; wherein, the outlet pipes of the respective deamination devices are respectively connected to the feed pipe of the latter deamination device, and the feed pipe of the first deamination device is used for introduction The low concentration ammonia water, the outlet pipe of the Nth deamination device is used to discharge a recycled water. The low-concentration ammonia deamination system described in claim 7 further includes a water outlet pipe connected to the outlet pipe of the N-th deamination device, wherein the water outlet pipe sequentially passes through the first N-1 The ammonia device is to the accommodating area of the first deamination device. The low-concentration ammonia deamination system described in claim 8 of the patent application further includes a pumping pump disposed at the end of the water outlet pipe for extracting the recovered water. An ammonia water production system comprising: a low-concentration ammonia water deamination system as described in claim 7 wherein the exhaust pipes of each deamination device are respectively connected to the upper portion of the evaporation zone of the previous deamination device; a condensing tank, a condenser is arranged in the middle of the condensing tank, a second accommodating area is formed at the bottom, and a second exhaust pipe is arranged at the top, and the exhaust pipe of the first deaminating device is connected to the lower side of the condenser The ammonia gas discharged from the exhaust pipe is condensed with the water gas to form a second low-concentration ammonia water, and the second low-concentration ammonia water is condensed and accommodated in the second accommodating area. a second outlet pipe is disposed in the second receiving area, the second exhaust pipe is configured to discharge an ammonia gas, and a pumping mixing unit is connected to the second exhaust pipe for extracting the ammonia gas and making the ammonia gas Dissolve Forming an ammonia water in the water; and an ammonia water tank connected to the air suction mixing unit for accommodating the ammonia water. The ammonia water production system according to claim 10, wherein the air suction mixing unit is a venturi tube, and the ammonia water production system further comprises a circulation line connecting the bottom of the ammonia water tank and the venturi, the cycle The pipeline is provided with a second pressure pump for extracting the ammonia water in the ammonia tank and pressurizing the venturi to extract the ammonia gas and dissolve the ammonia gas in the ammonia water. The ammonia water production system of claim 10, wherein the second outlet pipe is connected to the feed pipe of the first deamination device.