Device for removing oxygen from inlet water of heating and ventilation system
By designing a device for recycling waste heat using U-shaped tube condensation and screw tubes in the HVAC system, the problems of low temperature and high heating cost after deoxygenation in the prior art are solved, and rapid water source heating and resource conservation are achieved .
Patent Information
- Application Number
- CN202411517701.2
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2024-10-29
- Publication Date
- 2024-12-20
- Estimated Expiration
- 2044-10-29
AI Technical Summary
The existing HVAC system requires high temperature deoxygenation during the deoxygenation process, resulting in a low temperature after separation, which consumes a lot of resources to heat, increasing the cost of deoxygenation and injection into the HVAC system.
A device is designed to heat the water source and condense it through a U-shaped tube to separate the water from the air, and to recover waste heat using a screw tube to preheat the deoxygenated water source to reduce the heating loss of the HVAC system.
Through this device, the water source after deoxygenation can quickly reach the required temperature of the HVAC system, reducing the power consumption of HVAC and deoxygenation heating, and saving resources.
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Figure CN119160975A_ABST
Abstract
Description
Technical Field
[0001] The invention relates to the field of HVAC systems, and in particular to a device for deoxygenating incoming water in HVAC systems. Background Art
[0002] The HVAC system refers to the heating, gas supply, ventilation and air-conditioning engineering, which is an important part of the building. It aims to provide people with a comfortable, safe and energy-saving indoor environment. The working principle of the HVAC system is mainly based on a series of heat transfer, heat exchange and heat transmission processes. By controlling the temperature, flow and humidity of the air and other parameters, a comfortable environment is created for the room. Before adding water to the existing HVAC system, it is necessary to remove oxygen from the water source to prevent high-temperature water carrying oxygen from entering the pipe system, causing oxidation inside the pipe, thereby reducing the service life of the pipe.
[0003] The Chinese invention patent application with announcement number CN212987181U is a water replenishment and deoxygenation device for a new energy boiler, including a water supply tank, a booster pump is fixedly installed on the top surface of the water supply tank, and one end of the booster pump is connected to an air intake pipe, and the other end of the booster pump is connected to a U-shaped tube; in the utility model, the booster pump is turned on by the control panel, prompting the air intake pipe to guide the water vapor in the boiler into the U-shaped tube, and then discharged into the two comb-tooth type air injection pipes on the inner side of the water supply tank, so that the water vapor is discharged into the water supply tank through multiple air holes on the surface of the two air injection pipes, which is beneficial to the heat exchange between the water vapor and the liquid in the water supply tank, and can also disturb the liquid in the water tank in the form of bubbles. At the same time, the water vapor can increase the air pressure in the water supply tank, which is beneficial to the increase of the temperature in the water supply tank. By turning on the electric heating tube through the control panel, the double heating of the liquid in the water supply tank can be achieved, which is beneficial to the rapid increase of the temperature in the water supply tank, thereby increasing the deoxygenation efficiency.
[0004] During use, existing deoxygenation devices generally use high-temperature deoxygenation to separate oxygen. During separation, water vapor needs to be condensed to separate oxygen and other gases and water in the water source. However, the disadvantage of this method is that the water is at a relatively low temperature after separation. At this time, it takes a lot of resources to heat it when it is added to the HVAC system so that it is heated to the temperature required by the HVAC system. In addition, when water is added to the deoxygenation device, it also takes a lot of resources to heat it to an evaporating state, which greatly increases the cost of deoxygenation.
[0005] Therefore, it is necessary to invent a device for deoxygenating water entering a HVAC system to solve the above problems. Summary of the invention
[0006] The purpose of the present invention is to provide a device for deoxygenating water entering a HVAC system, by heating the water source and passing it through a U-shaped tube, and condensing it at the bend, so that water and air are separated, and the air containing residual temperature can enter the water source below through the spiral tube to recover the residual heat. At the same time, the deoxygenated water source can be preheated in the water source below and then injected into the HVAC system, thereby reducing the heating loss of the HVAC system, so as to solve the problem of high heating cost of water heating during the deoxygenation process and subsequent injection into the HVAC system in the prior art.
[0007] In order to achieve the above-mentioned purpose, the present invention provides the following technical solutions: a device for deoxygenating water entering a HVAC system, comprising a deoxygenating tank, a support leg is installed below the deoxygenating tank, a partition is installed on the inner wall of the deoxygenating tank, and the partition divides the deoxygenating tank into two upper and lower spaces, a pressure relief port is opened on the inner wall of the deoxygenating tank, a heating pipe is connected through the bottom of the deoxygenating tank, a water injection pipe is installed at the bottom of the deoxygenating tank, and the water injection pipe, the heating pipe and the pressure relief port are all arranged in the space below the deoxygenating tank;
[0008] A deoxygenation component is arranged above the interior of the deoxygenation tank and is used to remove oxygen from the water;
[0009] A stirring assembly is arranged at the lower part of the deaerator tank and is used to stir the water source;
[0010] The flow guide component is arranged below the partition plate and is used for guiding the steam.
[0011] As a preferred solution of the present invention, the deoxygenation component includes through holes, which are opened in the partition and are arranged in a ring-shaped distribution in multiple groups. Steam pipes are connected through the through holes, and the steam pipes are arranged in the upper space inside the deoxygenation tank. A connecting pipe is connected through one side of the steam pipe in a ring-shaped distribution, and the connecting pipe is connected to the remaining corresponding through holes, and this structure is arranged in a ring-shaped distribution in multiple groups on the partition.
[0012] As a preferred solution of the present invention, a condenser is installed on the top of the deaerator tank, an annular condenser is installed above the partition, and the annular condenser is connected to the condenser pipe, a U-shaped tube is connected above the steam pipe, and the annular condenser is penetrated and fitted with the turning parts of each group of U-shaped tubes.
[0013] As a preferred solution of the present invention, an L-shaped drain pipe is connected through the lowest point of the U-shaped pipe, and the L-shaped drain pipe is connected through the partition, and the L-shaped drain pipe is connected through the interior of the lower space inside the deaerator. An annular pipe 1 is installed below the outer side of the deaerator, and the annular pipe 1 is connected through each group of L-shaped drain pipes, and a drain pipe is connected through one side of the annular pipe 1.
[0014] As a preferred solution of the present invention, an annular pipe 2 is installed above the outer side of the deaerator, and the annular pipe 2 is connected with each group of U-shaped pipes, and one side of the annular pipe 2 is connected with the exhaust gas recovery device pipeline, a spiral pipe is installed in the space below the deaerator, a guide pipe is installed between the spiral pipe and the annular pipe 2, and a control valve is installed in the guide pipe, and the spiral pipe and the L-shaped drain pipe are immersed in the water source in the space below the deaerator.
[0015] As a preferred solution of the present invention, the stirring assembly includes a motor, which is installed above the partition and located in the space above the deaerator. A main stirring rod is installed at the output end of the motor and is arranged in the space below the deaerator.
[0016] As a preferred solution of the present invention, an annular frame is installed above the main stirring rod, a main draft tube is installed below the partition, and the interior of the main draft tube completely covers all the through holes.
[0017] As a preferred solution of the present invention, a gear ring 1 is installed on the inner wall of the main flow tube, four groups of auxiliary stirring rods are rotatably connected below the annular frame, a gear ring 2 is installed above the annular frame, gears 1 are sleeved and fixed on the four groups of auxiliary stirring rods, and the four groups of gears 1 are meshed with gear ring 1.
[0018] As a preferred solution of the present invention, the guide assembly includes an auxiliary guide tube, which is installed in a ring-shaped distribution below the partition, and the auxiliary guide tube covers each group of through holes separately. A turbofan is installed in the auxiliary guide tube, and a gear two is connected to the shaft below the turbofan, and each group of gears two is meshed with gear ring two.
[0019] In the above technical solution, compared with the prior art, the technical effects and advantages provided by the present invention are as follows:
[0020] The water source is vaporized and transported to the U-shaped tube, and the gas is condensed and liquefied at the lowest point of the U-shaped tube, thereby removing the air inside and completing the deoxygenation work. At this time, the deoxygenated water is diverted through the high-temperature water source under the deoxygenation tank that is in the process of vaporization, so as to preheat the water source, and the discharged air after deoxygenation contains a certain temperature. At this time, when the temperature in the high-temperature water source under the deoxygenation tank that is in the process of vaporization is low, the air discharged after deoxygenation can enter the water source under the deoxygenation tank through the spiral tube, so as to recover the waste heat. This structure can ensure that the deoxygenated water source can quickly reach the water temperature required by the HVAC system, reduce the power consumption of HVAC heating and deoxygenation heating, and achieve the purpose of saving resources. BRIEF DESCRIPTION OF THE DRAWINGS
[0021] In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the drawings required for use in the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments recorded in the present invention. For ordinary technicians in this field, other drawings can also be obtained based on these drawings.
[0022] Figure 1 It is a schematic diagram of the overall structure of the present invention;
[0023] Figure 2 It is a schematic diagram of the U-shaped tube planing structure of the present invention;
[0024] Figure 3 It is a schematic diagram of the bottom structure of the partition of the present invention;
[0025] Figure 4 It is a schematic diagram of the layout structure of the main stirring rod and the auxiliary stirring rod of the present invention;
[0026] Figure 5 It is a schematic diagram of the planed structure of the deaerator tank of the present invention;
[0027] Figure 6 For the present invention Figure 2 The enlarged structural diagram at A in the middle;
[0028] Figure 7 For the present invention Figure 3 The enlarged structural diagram at B in the middle;
[0029] Figure 8 For the present invention Figure 4 Enlarged structural diagram at point C in the middle.
[0030] Description of reference numerals:
[0031] 001, deaerator tank; 101, support leg; 102, partition; 103, pressure relief port; 104, heating pipe; 105, water injection pipe; 002, deaerator assembly; 201, through hole; 202, steam pipe; 203, connecting pipe; 204, U-shaped pipe; 205, L-shaped drain pipe; 206, annular pipe one; 207, annular pipe two; 208, spiral pipe; 209, guide pipe; 210, drain pipe; 211, condenser; 212, annular condenser; 003, stirring assembly; 301, motor; 302, main stirring rod; 303, annular frame; 304, main draft tube; 305, gear ring one; 306, auxiliary stirring rod; 307, gear one; 004, guide assembly; 401, auxiliary guide tube; 402, turbofan; 403, gear two; 404, gear ring two. DETAILED DESCRIPTION
[0032] In order to enable those skilled in the art to better understand the technical solution of the present invention, the present invention will be further described in detail below with reference to the accompanying drawings.
[0033] The present invention provides Figure 1-8 A device for deoxygenating water entering a HVAC system is shown, comprising a deoxygenation tank 001, a support leg 101 is installed below the deoxygenation tank 001, a partition 102 is installed on the inner wall of the deoxygenation tank 001, and the partition 102 divides the deoxygenation tank 001 into two upper and lower spaces, a pressure relief port 103 is opened on the inner wall of the deoxygenation tank 001, a heating pipe 104 is connected through the bottom of the deoxygenation tank 001, a water injection pipe 105 is installed at the bottom of the deoxygenation tank 001, and the water injection pipe 105, the heating pipe 104 and the pressure relief port 103 are all arranged in the space below the deoxygenation tank 001;
[0034] Water can be injected into the space below the deaerator tank 001 through the water injection pipe 105, and the heating pipe 104 can inject heat to heat the water. When the pressure is high, the pressure relief port 103 can be opened to relieve the pressure in the deaerator tank 001 to ensure safe deoxygenation.
[0035] The deoxygenation component 002 is disposed above the deoxygenation tank 001 and is used to remove oxygen from the water;
[0036] The stirring assembly 003 is disposed at the lower part of the deaerator tank 001 and is used to stir the water source;
[0037] The flow guide component 004 is arranged below the partition 102 and is used for guiding the steam.
[0038] Furthermore, in the above structure, the deoxygenation component 002 includes a through hole 201, which is opened in the partition 102 and is arranged in a ring-shaped distribution. A steam pipe 202 is connected through the through hole 201, and the steam pipe 202 is arranged in the upper space inside the deoxygenation tank 001. A connecting pipe 203 is connected through one side of the steam pipe 202 in a ring-shaped distribution, and the connecting pipe 203 is connected to the remaining corresponding through holes 201, and this structure is arranged in a ring-shaped distribution on the partition 102.
[0039] The steam in the space below the deaerator tank 001 can enter the steam pipe 202 and the connecting pipe 203 through the through hole 201 .
[0040] Furthermore, in the above structure, a condenser 211 is installed on the top of the deoxygenation tank 001, an annular condenser tube 212 is installed above the partition 102, and the annular condenser tube 212 is connected to the condenser 211 pipeline, a U-shaped tube 204 is connected through the top of the steam pipe 202, and the annular condenser tube 212 is penetrated and fitted with the turning parts of each group of U-shaped tubes 204.
[0041] Through the condenser 211, the annular condenser tube 212 can perform condensation work at the turning point of the U-shaped tube 204. At this time, the steam passing through the U-shaped tube 204 will be liquefied due to the condensation, and the internal gas will continue to be transported along the U-shaped tube 204, thereby completing the oxygen removal work in the water source.
[0042] Furthermore, in the above structure, an L-shaped drain pipe 205 is connected through the lowest point of the U-shaped pipe 204, and the L-shaped drain pipe 205 penetrates the partition 102, and the L-shaped drain pipe 205 is connected through the interior of the lower space inside the deaerator tank 001. An annular pipe 206 is installed below the outer side of the deaerator tank 001, and the annular pipe 206 is connected through each group of L-shaped drain pipes 205, and a drain pipe 210 is connected through one side of the annular pipe 206.
[0043] The condensed and liquefied water source can be collected through the L-shaped drain pipe 205 and transported through the lower space inside the deaerator tank 001. At this time, due to the high-temperature water source in the space below the deaerator tank 001, the liquefied water source can be heated to increase its temperature or return to normal temperature to avoid its low temperature after deoxygenation. Finally, it enters the annular pipe 206 and is transported to the heating system by the drain pipe 210.
[0044] Furthermore, in the above structure, a second annular pipe 207 is installed above the outer side of the deaerator tank 001, and the second annular pipe 207 is connected with each group of U-shaped pipes 204, and one side of the second annular pipe 207 is connected with the exhaust gas recovery device pipeline, a spiral pipe 208 is installed in the space below the deaerator tank 001, a guide pipe 209 is installed between the spiral pipe 208 and the second annular pipe 207, and a control valve is installed in the guide pipe 209, and the spiral pipe 208 and the L-shaped drain pipe 205 are immersed in the water source in the space below the deaerator tank 001.
[0045] The gas can be transported to the annular pipe 207 through the U-shaped pipe 204. At this time, since the gas in the annular pipe 207 still has a certain temperature, when new water is injected under the deaerator tank 001, the temperature is relatively low, and the gas can be transported to the spiral pipe 208 to heat the newly injected water. When heated to a higher temperature, the guide pipe 209 can be closed so that the gas can be discharged normally.
[0046] Furthermore, in the above structure, the stirring assembly 003 includes a motor 301, which is installed above the partition 102 and located in the space above the deaerator tank 001. A main stirring rod 302 is installed at the output end of the motor 301, and the main stirring rod 302 is arranged in the space below the deaerator tank 001.
[0047] The motor 301 can drive the main stirring rod 302 to rotate in the space below the deaerator tank 001, thereby stirring the water source and increasing the efficiency of water source heating.
[0048] Furthermore, in the above structure, an annular frame 303 is installed above the main stirring rod 302 , a main draft tube 304 is installed below the partition 102 , and the interior of the main draft tube 304 completely covers all the through holes 201 .
[0049] The main flow tube 304 allows the water vapor generated by the water source to smoothly enter the area where the through hole 201 is located.
[0050] Furthermore, in the above structure, a gear ring 305 is installed on the inner wall of the main flow tube 304, four groups of auxiliary stirring rods 306 are rotatably connected below the annular frame 303, a gear ring 2 404 is installed above the annular frame 303, gears 307 are sleeved and fixed on the four groups of auxiliary stirring rods 306, and the four groups of gears 307 are meshed with the gear ring 305.
[0051] The gear 1 307 slides along the gear ring 2 404 , so that the auxiliary stirring rod 306 can rotate as a whole under the action of the annular frame 303 and can rotate on its own, thereby improving the stirring effect.
[0052] Furthermore, in the above structure, the guide assembly 004 includes an auxiliary guide tube 401, which is installed in a ring-shaped distribution below the partition 102, and the auxiliary guide tube 401 covers each group of through holes 201 separately. A turbofan 402 is installed in the auxiliary guide tube 401, and a gear 2 403 is connected to the axis below the turbofan 402, and each group of gear 2 403 is meshed with a gear ring 2 404.
[0053] By setting the auxiliary guide tube 401, the gear ring 2 404 can drive the turbofan 402 to rotate under the action of the annular frame 303, so that water vapor enters the auxiliary guide tube 401, thereby accurately delivering the water vapor into the through hole 201 and improving the efficiency of water vapor transportation.
[0054] like Figure 1-8As shown, water can be injected into the space below the deaerator tank 001 through the water injection pipe 105. At this time, the heating pipe 104 heats the water source. At the same time, the motor 301 drives the main stirring rod 302 and the auxiliary stirring rod 306 to rotate, thereby stirring the water source to increase the heating efficiency. At the same time, the turbofan 402 rotates in the auxiliary guide tube 401 to guide the water vapor generated by the water source, so that the water vapor enters the steam pipe 202 and the connecting pipe 203 through the through hole 201. When passing through the bend of the U-shaped pipe 204, the water vapor is condensed into water under the condensation effect of the annular condenser 212, and enters the annular pipe 206 through the L-shaped drain pipe 205. At the same time, the deoxygenated Air will be continuously transported to the annular pipe 207, and when the temperature of the water source below the deaerator tank 001 is low, the residual heat of the deoxygenated air can be transferred to the water source below the deaerator tank 001 through the spiral tube 208. Otherwise, it will be discharged normally to realize heat energy recovery and reduce the cost of deoxygenation. The water in the L-shaped drain pipe 205 will pass through the water source in the space below the deaerator tank 001, thereby preheating the water in the L-shaped drain pipe 205 so that it can quickly heat up when it enters the HVAC system, thereby reducing resources. This structure can ensure that the deoxygenated water source can quickly reach the water temperature required by the HVAC system, reduce the power consumption of HVAC heating and deoxygenation heating, and achieve the purpose of saving resources.
[0055] The above description is only by way of illustration of certain exemplary embodiments of the present invention. It is undoubted that those skilled in the art can modify the described embodiments in various ways without departing from the spirit and scope of the present invention. Therefore, the above drawings and descriptions are illustrative in nature and should not be construed as limiting the scope of protection of the claims of the present invention.
Claims
1. A device for deoxygenating water entering a heating and ventilation system, comprising a deoxygenation tank (001), characterized in that: A support leg (101) is installed below the deaerator (001); a partition (102) is installed on the inner wall of the deaerator (001), and the partition (102) divides the deaerator (001) into two upper and lower spaces; a pressure relief port (103) is opened on the inner wall of the deaerator (001); a heating pipe (104) is connected through the bottom of the deaerator (001); a water injection pipe (105) is installed at the bottom of the deaerator (001), and the water injection pipe (105), the heating pipe (104) and the pressure relief port (103) are all arranged in the space below the deaerator (001); A deoxygenation component (002) is disposed above the interior of the deoxygenation tank (001) and is used to remove oxygen from the water; A stirring assembly (003) is disposed at the lower part of the deaerator tank (001) and is used to stir the water source; The flow guide component (004) is arranged below the partition (102) and is used to guide the steam.
2. The device for deoxygenating water entering a HVAC system according to claim 1, characterized in that: The deoxidation component (002) comprises through holes (201), the through holes (201) are provided in the partition (102), and a plurality of through holes (201) are provided in an annular distribution. A steam pipe (202) is connected through the through holes (201), and the steam pipe (202) is arranged in the upper space inside the deoxidation tank (001). A connecting pipe (203) is connected through one side of the steam pipe (202) in an annular distribution, and the connecting pipe (203) is connected through the other corresponding through holes (201), and a plurality of such structures are provided in an annular distribution on the partition (102).
3. The device for deoxygenating water in a HVAC system according to claim 2, characterized in that: A condenser (211) is installed on the top of the deaerator tank (001), an annular condenser pipe (212) is installed above the partition (102), and the annular condenser pipe (212) is connected to the condenser (211) pipeline, a U-shaped pipe (204) is connected through the top of the steam pipe (202), and the annular condenser pipe (212) penetrates and fits with the turning parts of each group of U-shaped pipes (204).
4. The device for deoxygenating water entering a HVAC system according to claim 3, characterized in that: The lowest part of the U-shaped pipe (204) is connected to an L-shaped drainage pipe (205), and the L-shaped drainage pipe (205) is connected to the partition (102), and the L-shaped drainage pipe (205) is connected to the interior of the lower space inside the deaerator (001). An annular pipe (206) is installed below the outer side of the deaerator (001), and the annular pipe (206) is connected to each group of L-shaped drainage pipes (205). One side of the annular pipe (206) is connected to a drainage pipe (210).
5. The device for deoxygenating water entering a HVAC system according to claim 4, characterized in that: A second annular pipe (207) is installed above the outer side of the deaerator (001), and the second annular pipe (207) is connected to each group of U-shaped pipes (204), and one side of the second annular pipe (207) is connected to the pipeline of the exhaust gas recovery device. A spiral pipe (208) is installed in the space below the deaerator (001), and a guide pipe (209) is installed between the spiral pipe (208) and the second annular pipe (207), and a control valve is installed in the guide pipe (209), and the spiral pipe (208) and the L-shaped drainage pipe (205) are immersed in the water source in the space below the deaerator (001).
6. The device for deoxygenating water entering a HVAC system according to claim 1, characterized in that: The stirring assembly (003) comprises a motor (301), wherein the motor (301) is installed above the partition (102), and the motor (301) is located in the space above the deaerator (001); a main stirring rod (302) is installed at the output end of the motor (301), and the main stirring rod (302) is arranged in the space below the deaerator (001).
7. The device for deoxygenating water entering a HVAC system according to claim 6, characterized in that: An annular frame (303) is installed above the main stirring rod (302), a main draft tube (304) is installed below the partition (102), and the interior of the main draft tube (304) completely covers all the through holes (201).
8. The device for deoxygenating water entering a HVAC system according to claim 7, characterized in that: A gear ring 1 (305) is installed on the inner wall of the main flow tube (304), four groups of auxiliary stirring rods (306) are rotatably connected below the annular frame (303), a gear ring 2 (404) is installed above the annular frame (303), gears 1 (307) are sleeved and fixed on the four groups of auxiliary stirring rods (306), and the four groups of gears 1 (307) are meshed with the gear ring 1 (305).
9. The device for deoxygenating water entering a HVAC system according to claim 1, characterized in that: The flow guide assembly (004) comprises a secondary flow guide tube (401), which is installed in a ring-shaped distribution below the partition (102), and the secondary flow guide tube (401) covers each group of through holes (201) separately. A turbofan (402) is installed in the secondary flow guide tube (401), and a gear 2 (403) is connected to the shaft below the turbofan (402), and each group of gear 2 (403) is meshed with a gear ring 2 (404).
Citation Information
Patent Citations
Water replenishing and deoxidizing device for new energy boiler
CN212987181U
Steam heat recovery heating system for thermal deaerator
CN214370089U
Exhaust steam waste heat recovery device of deaerator
CN220911434U
