CN221156002U - Dirty useless argon gas recovery enrichment facility of argon gas recovery intercooler tank discharge - Google Patents
Dirty useless argon gas recovery enrichment facility of argon gas recovery intercooler tank discharge Download PDFInfo
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- CN221156002U CN221156002U CN202323230082.2U CN202323230082U CN221156002U CN 221156002 U CN221156002 U CN 221156002U CN 202323230082 U CN202323230082 U CN 202323230082U CN 221156002 U CN221156002 U CN 221156002U
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- argon
- recycling
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- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 title claims abstract description 110
- 239000007789 gas Substances 0.000 title claims abstract description 67
- 229910052786 argon Inorganic materials 0.000 title claims abstract description 55
- 238000011084 recovery Methods 0.000 title claims description 14
- 238000001179 sorption measurement Methods 0.000 claims abstract description 92
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 50
- 238000004064 recycling Methods 0.000 claims abstract description 29
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 22
- 239000002699 waste material Substances 0.000 claims abstract description 18
- 239000002245 particle Substances 0.000 claims abstract description 11
- 229910001873 dinitrogen Inorganic materials 0.000 claims description 6
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 3
- 239000007863 gel particle Substances 0.000 claims description 3
- 229910052710 silicon Inorganic materials 0.000 claims description 3
- 239000010703 silicon Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 claims description 2
- 238000007789 sealing Methods 0.000 claims description 2
- 229920002379 silicone rubber Polymers 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 16
- 238000009434 installation Methods 0.000 abstract description 15
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 9
- 239000000741 silica gel Substances 0.000 abstract description 9
- 229910002027 silica gel Inorganic materials 0.000 abstract description 9
- 238000001816 cooling Methods 0.000 abstract description 5
- 238000000746 purification Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 4
- 239000000126 substance Substances 0.000 abstract description 4
- 239000003463 adsorbent Substances 0.000 description 11
- 230000008929 regeneration Effects 0.000 description 6
- 238000011069 regeneration method Methods 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- PWKWDCOTNGQLID-UHFFFAOYSA-N [N].[Ar] Chemical compound [N].[Ar] PWKWDCOTNGQLID-UHFFFAOYSA-N 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229910001338 liquidmetal Inorganic materials 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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- Separation Of Gases By Adsorption (AREA)
Abstract
The utility model discloses a device for recycling and concentrating dirty and waste argon discharged by an argon recycling middle cooling box, which belongs to the technical field of argon recycling and purifying and comprises a pressurizing assembly for pressurizing mixed gas, a buffer assembly (3) for maintaining stable gas pressure, a double-station adsorption assembly for adsorbing nitrogen and an exhaust assembly for exhausting gas, wherein the pressurizing assembly is connected with the buffer assembly (3), the buffer assembly (3) is connected with the double-station adsorption assembly, and the double-station adsorption assembly is connected with the exhaust assembly; the exhaust assembly includes a nitrogen exhaust assembly and a control valve E (10). Through the mode, the water in the mixed gas can be removed through the dried silica gel particles, and meanwhile, when the water removing effect of the silica gel particles is weakened, a new installation box (37) can be replaced; argon can be purified all the time, and adsorption purification does not need to be suspended because of saturation of adsorption substances.
Description
Technical Field
The utility model relates to the technical field of argon recovery and purification, in particular to a device for recovering and concentrating dirty and waste argon discharged from an argon recovery middle cooling box.
Background
Argon is an inert gas which does not react with other substances at normal temperature, is insoluble in liquid metal at high temperature, can show superiority when welding nonferrous metal, and can be used for bulb inflation and arc welding of stainless steel, magnesium, aluminum and the like.
Chinese patent CN217929405U discloses an argon purification device for argon gas tail gas recovery, including bottom plate and buffer gear, the top fixedly connected with air pump of bottom plate, the air inlet of air pump communicates and is fixed with same second L-shaped pipe between the bottom of hose, the top fixedly connected with water cooler of bottom plate, the gas outlet of air pump communicates and is fixed with same third L-shaped pipe between the left side of water cooler, the top fixedly connected with clarifier of bottom plate, communicate and is fixed with same first connecting pipe between water cooler and the clarifier, the top fixedly connected with rectifying column of bottom plate, communicate and be fixed with same second connecting pipe between the left side of rectifying column and the right side of clarifier, start the air pump, the air pump work is taken out gas through first L-shaped pipe, hose and second L-shaped pipe, discharge gas into the water cooler through the third L-shaped pipe, the water cooler carries out the cooling treatment to gas, the gas after the cooling enters into the clarifier through first connecting pipe in, the carbon dioxide in the gas is got rid of, gas gets into the rectifying column through the second connecting pipe in, thereby obtain pure argon bottom in rectifying column.
But this patent fails to remove moisture from the tail gas.
Based on the above, the utility model designs a device for recycling and concentrating the polluted and waste argon discharged from the cold box in the argon recycling process to solve the problems.
Disclosure of utility model
Aiming at the defects existing in the prior art, the utility model provides a device for recycling and concentrating the polluted and waste argon discharged from an argon recycling middle cooling box.
In order to achieve the above purpose, the utility model is realized by the following technical scheme:
An argon recovery and concentration device for discharging dirty and waste argon from an argon recovery intercooler tank;
The device comprises a pressurizing assembly for pressurizing the mixed gas, a buffer assembly (3) for maintaining the pressure stability of the gas, a double-station adsorption assembly for adsorbing nitrogen and an exhaust assembly for exhausting the gas, wherein the pressurizing assembly is connected with the buffer assembly (3), the buffer assembly (3) is connected with the double-station adsorption assembly, and the double-station adsorption assembly is connected with the exhaust assembly;
The exhaust assembly includes a nitrogen exhaust assembly and a control valve E (10).
Furthermore, the supercharging assembly comprises a supercharging device (1) and a control valve group H (2), the air inlet end of the supercharging device (1) is communicated with the external mixed gas supply end, the air inlet end and the air outlet end of the supercharging device (1) are respectively communicated with the two ends of the control valve group H (2), and the air outlet end of the supercharging device (1) is connected with the buffer assembly (3).
Still further, buffer unit (3) include intake pipe (31), end cover (32), mount pad (33), jar body (34), outlet duct (35), spout (36), install bin (37) and air vent (38), the inlet end fixedly connected with mount pad (33) of jar body (34), the end cover (32) can be dismantled to the inlet end of mount pad (33), the inlet end fixedly connected with intake pipe (31) of end cover (32), the inlet pipe (31) communicates with supercharging device (1)'s the end of giving vent to anger, a plurality of spouts (36) have been seted up to the inside circumference array of jar body (34), a plurality of air vents (38) have all been seted up at the outer end embedding spout (36) of install bin (37) and with jar body (34) sliding connection, the inside packing of install bin (37) has dry silica gel particle, outlet duct (35) and duplex adsorption unit intercommunication.
Further, the diameter of the vent hole (38) is smaller than the diameter of the silicon gel particle.
Furthermore, a detector for detecting the moisture of the mixed gas is fixedly arranged in the air outlet pipe (35).
Furthermore, the air inlet end of the mounting seat (33) is detachably connected with a tank body (34) through a screw.
Further, a sealing ring is arranged between the end cover (32) and the mounting seat (33).
Still further, duplex adsorption component includes control valve A (4), first adsorption tower (5), control valve B (6), control valve C (7), second adsorption tower (8) and control valve D (9), the end of giving vent to anger of control valve A (4) communicates with the inlet end of first adsorption tower (5), the end of giving vent to anger of first adsorption tower (5) communicates with the inlet end of control valve B (6), the end of giving vent to anger of control valve C (7) communicates with the inlet end of second adsorption tower (8), the end of giving vent to anger of second adsorption tower (8) communicates with the inlet end of control valve D (9), the inlet ends of first adsorption tower (5) and second adsorption tower (8) all are connected with nitrogen gas exhaust component, the end of giving vent to anger of control valve B (6) and control valve D (9) all communicates with control valve E (10).
Furthermore, the air inlet ends of the control valve A (4) and the control valve C (7) are communicated with the air outlet pipe (35).
Still further, nitrogen gas exhaust subassembly includes control valve F (11), control valve G (12) and vacuum pump (13), and the inlet end of control valve F (11) and control valve G (12) communicates with the inlet end of first adsorption tower (5) and second adsorption tower (8) respectively, and the outlet end of control valve F (11) and control valve G (12) all communicates with the inlet end of vacuum pump (13).
The utility model has the following technical effects:
when the utility model is used for pressurizing, nitrogen-argon mixed gas is introduced into the concentration device from an external mixed gas supply end, a control valve group H (2) is opened, the mixed gas enters the pressurizing device (1) through an air inlet pipe and is pressurized to a required pressure, and then enters the buffer assembly (3) to stabilize the pressure of the mixed gas and remove water;
After the mixed gas is discharged from the air outlet end of the supercharging device (1), the mixed gas enters the tank body (34) from the air inlet pipe (31), when the mixed gas passes through the mounting box (37), the dry silica gel particles in the mounting box (37) remove water from the mixed gas, and finally the mixed gas is discharged from the air outlet pipe (35);
When the detector at the inner end of the air outlet pipe (35) detects that the water content in the mixed gas is increased, the installation box (37) needs to be replaced, the end cover (32) is detached, the installation box (37) is taken out from the tank body (34), the protruding block of the new installation box (37) is aligned with the sliding groove (36), the installation box (37) is pressed, the installation box (37) is completely embedded into the groove (44), and finally the detached end cover (32) is reinstalled on the installation seat (33) to complete replacement.
According to the utility model, the water in the mixed gas can be removed through the dried silica gel particles, and meanwhile, when the water removing effect of the silica gel particles is weakened, a new installation box (37) can be replaced;
When the nitrogen is adsorbed, a control valve A (4) is opened, mixed gas enters a first adsorption tower (5) through an air inlet pipe, nitrogen in the mixed gas is physically adsorbed by an adsorbent in the first adsorption tower (5), a control valve B (6) and a control valve E (10) are opened, residual enriched argon is discharged, the discharged gas is stored or enters other devices, when the adsorbent in the first adsorption tower (5) is nearly saturated with the nitrogen, the valves at the air inlet end and the air outlet end of the first adsorption tower (5) are controlled by a computer, a control valve C (7) is opened, the mixed gas enters a second adsorption tower (8) through the air inlet pipe, the nitrogen in the mixed gas is physically adsorbed by the adsorbent in the second adsorption tower (8), a control valve D (9) and a control valve E (10) are opened, the residual enriched argon is discharged, and the first adsorption tower (5) is switched to the first adsorption tower (5) for adsorption after the regeneration is completed;
The utility model can always purify the argon, and the adsorption purification can not be stopped because of the saturation of the adsorption substances;
When the first adsorption tower (5) needs to be regenerated, after the front and rear valves of the first adsorption tower (5) are completely closed, the control valve F (11) is opened, then the vacuum pump (13) is started, nitrogen which is physically adsorbed by the adsorbent in the first adsorption tower (5) is pumped out, after the nitrogen is completely pumped out (the vacuum degree is about- (5) kpa), the regeneration of the first adsorption tower (5) is completed, when the second adsorption tower (8) needs to be regenerated, after the front and rear valves of the second adsorption tower (8) are completely closed, the control valve G (12) is opened, the control valve F (11) is closed, then the vacuum pump (13) is started, and the nitrogen which is physically adsorbed by the adsorbent in the second adsorption tower (8) is completely pumped out, so that the regeneration of the second adsorption tower (8) is completed.
Drawings
In order to more clearly illustrate the embodiments of the present utility model or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below. It is evident that the drawings in the following description are only some embodiments of the present utility model and that other drawings may be obtained from these drawings without inventive effort for a person of ordinary skill in the art.
FIG. 1 is a block diagram I of a device for recycling and concentrating dirty and waste argon discharged by an argon recycling intercooler tank;
FIG. 2 is a perspective view I of a buffer assembly of the device for recycling and concentrating dirty and waste argon discharged from an argon recycling intercooler tank;
FIG. 3 is a front view of a buffer assembly of an argon recovery intercooler exhaust dirty waste argon recovery concentrating device of the present utility model;
FIG. 4 is a perspective view of a buffer assembly II of the device for recycling and concentrating dirty and waste argon discharged from the argon recycling intercooler tank;
fig. 5 is a cross-sectional view taken along the A-A direction of fig. 3.
Reference numerals in the drawings represent respectively:
1. A supercharging device; 2. a control valve group H; 3. a buffer assembly; 31. an air inlet pipe; 32. an end cap; 33. a mounting base; 34. a tank body; 35. an air outlet pipe; 36. a chute; 37. a mounting box; 38. a vent hole; 4. a control valve A; 5. a first adsorption tower; 6. a control valve B; 7. a control valve C; 8. a second adsorption tower; 9. a control valve D; 1. a control valve E; 11. a control valve F; 12. a control valve G; 13. and a vacuum pump.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present utility model more clear, the technical solutions of the embodiments of the present utility model will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present utility model. It will be apparent that the described embodiments are some, but not all, embodiments of the utility model. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
The utility model is further described below with reference to examples.
Reference to "left", "right", "front", "rear", "upper", "lower" in the following description is oriented in the viewing direction of the front view.
Example 1
Referring to the attached drawings 1-5 in the specification, a device for recycling and concentrating dirty and waste argon discharged by an argon recycling intercooler tank;
The device comprises a pressurizing assembly for pressurizing the mixed gas, a buffer assembly (3) for maintaining the pressure stability of the gas, a double-station adsorption assembly for adsorbing nitrogen and an exhaust assembly for exhausting the gas, wherein the pressurizing assembly is connected with the buffer assembly (3), the buffer assembly (3) is connected with the double-station adsorption assembly, and the double-station adsorption assembly is connected with the exhaust assembly;
The exhaust assembly includes a nitrogen exhaust assembly and a control valve E (10).
The supercharging assembly comprises a supercharging device (1) and a control valve group H (2), wherein the air inlet end of the supercharging device (1) is communicated with the external mixed gas supply end, the air inlet end and the air outlet end of the supercharging device (1) are respectively communicated with the two ends of the control valve group H (2), and the air outlet end of the supercharging device (1) is connected with the buffering assembly (3).
During pressurization, nitrogen-argon mixed gas is introduced into the concentration device from an external mixed gas supply end, a control valve group H (2) is opened, the mixed gas enters a pressurizing device (1) through an air inlet pipe, is pressurized to a required pressure, and then enters a buffer assembly (3), and the mixed gas is stabilized in pressure and moisture is removed;
The buffer assembly (3) comprises an air inlet pipe (31), an end cover (32), a mounting seat (33), a tank body (34), an air outlet pipe (35), a sliding groove (36), a mounting box (37) and an air vent (38), wherein the air inlet end of the tank body (34) is fixedly connected with the mounting seat (33), the air inlet end of the mounting seat (33) is detachably connected with the end cover (32), the air inlet end of the end cover (32) is fixedly connected with the air inlet pipe (31), the air inlet pipe (31) is communicated with the air outlet end of the supercharging device (1), the air outlet end of the tank body (34) is fixedly connected with the air outlet pipe (35), a plurality of sliding grooves (36) are formed in an inner circumferential array of the tank body (34), the outer end of the mounting box (37) is embedded in the sliding groove (36) and is in sliding connection with the tank body (34), a plurality of air vents (38) are formed in two ends of the mounting box (37), dry silicon rubber particles are filled in the mounting box (37), and the air outlet pipe (35) is communicated with the double-station adsorption assembly.
The diameter of the vent hole (38) is smaller than the diameter of the silicon gel particle.
Preferably, a detector for detecting the moisture of the mixed gas is fixedly arranged in the air outlet pipe (35).
After the mixed gas is discharged from the air outlet end of the supercharging device (1), the mixed gas enters the tank body (34) from the air inlet pipe (31), when the mixed gas passes through the mounting box (37), the dry silica gel particles in the mounting box (37) remove water from the mixed gas, and finally the mixed gas is discharged from the air outlet pipe (35);
When the detector at the inner end of the air outlet pipe (35) detects that the water content in the mixed gas is increased, the installation box (37) needs to be replaced, the end cover (32) is detached, the installation box (37) is taken out from the tank body (34), the protruding block of the new installation box (37) is aligned with the sliding groove (36), the installation box (37) is pressed, the installation box (37) is completely embedded into the groove (44), and finally the detached end cover (32) is reinstalled on the installation seat (33) to complete replacement.
According to the utility model, the water in the mixed gas can be removed through the dried silica gel particles, and meanwhile, when the water removing effect of the silica gel particles is weakened, a new installation box (37) can be replaced;
The double-station adsorption assembly comprises a control valve A (4), a first adsorption tower (5), a control valve B (6), a control valve C (7), a second adsorption tower (8) and a control valve D (9), wherein the air outlet end of the control valve A (4) is communicated with the air inlet end of the first adsorption tower (5), the air outlet end of the first adsorption tower (5) is communicated with the air inlet end of the control valve B (6), the air outlet end of the control valve C (7) is communicated with the air inlet end of the second adsorption tower (8), the air outlet end of the second adsorption tower (8) is communicated with the air inlet end of the control valve D (9), the air inlet ends of the first adsorption tower (5) and the second adsorption tower (8) are connected with the nitrogen gas exhaust assembly, and the air outlet ends of the control valve B (6) and the control valve D (9) are communicated with a control valve E (10).
The first adsorption tower (5) and the second adsorption tower (8) are filled with adsorbents of crystal materials with three-dimensional network structures.
The air inlet ends of the control valve A (4) and the control valve C (7) are communicated with an air outlet pipe (35).
When nitrogen is adsorbed, a control valve A (4) is opened, mixed gas enters a first adsorption tower (5) through an air inlet pipe, nitrogen in the mixed gas is physically adsorbed by an adsorbent in the first adsorption tower (5), a control valve B (6) and a control valve E (10) are opened, residual enriched argon is discharged, discharged gas is stored or enters other devices, when the adsorbent in the first adsorption tower (5) is nearly saturated with the nitrogen, the valves at the air inlet end and the air outlet end of the first adsorption tower (5) are controlled by a computer, a control valve C (7) is opened, the mixed gas enters a second adsorption tower (8) through the air inlet pipe, the nitrogen in the mixed gas is physically adsorbed by the adsorbent in the second adsorption tower (8), a control valve D (9) and a control valve E (10) are opened, and the residual enriched argon is discharged, and is switched to the first adsorption tower (5) for adsorption after the regeneration of the first adsorption tower (5) is completed;
The utility model can always purify the argon, and the adsorption purification can not be stopped because of the saturation of the adsorption substances;
The nitrogen gas exhaust assembly comprises a control valve F (11), a control valve G (12) and a vacuum pump (13), wherein the air inlet ends of the control valve F (11) and the control valve G (12) are respectively communicated with the air inlet ends of the first adsorption tower (5) and the second adsorption tower (8), and the air outlet ends of the control valve F (11) and the control valve G (12) are respectively communicated with the air inlet end of the vacuum pump (13).
When the first adsorption tower (5) needs to be regenerated, after the front and rear valves of the first adsorption tower (5) are completely closed, the control valve F (11) is opened, then the vacuum pump (13) is started, nitrogen which is physically adsorbed by the adsorbent in the first adsorption tower (5) is pumped out, after the nitrogen is completely pumped out (the vacuum degree is about- (5) kpa), the regeneration of the first adsorption tower (5) is completed, when the second adsorption tower (8) needs to be regenerated, after the front and rear valves of the second adsorption tower (8) are completely closed, the control valve G (12) is opened, the control valve F (11) is closed, then the vacuum pump (13) is started, and the nitrogen which is physically adsorbed by the adsorbent in the second adsorption tower (8) is completely pumped out, so that the regeneration of the second adsorption tower (8) is completed.
Example 2
As shown in fig. 1 to 5, as a preferred embodiment of the present utility model, the air inlet end of the mount (33) is preferably detachably connected to the tank (34) by screws.
Example 3
As shown in fig. 1-5, as a preferred embodiment of the present utility model, a seal ring is preferably mounted between the end cap (32) and the mounting base (33).
The above embodiments are only for illustrating the technical solution of the present utility model, and are not limiting; although the utility model has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical scheme described in the foregoing embodiments can be modified or some technical features thereof can be replaced by equivalents; such modifications and substitutions do not depart from the spirit and scope of the technical solutions of the embodiments of the present utility model.
Claims (10)
1. The utility model provides an dirty useless argon gas recovery enrichment facility of argon gas recovery intercooler tank discharge which characterized in that:
The device comprises a pressurizing assembly for pressurizing the mixed gas, a buffer assembly (3) for maintaining the pressure stability of the gas, a double-station adsorption assembly for adsorbing nitrogen and an exhaust assembly for exhausting the gas, wherein the pressurizing assembly is connected with the buffer assembly (3), the buffer assembly (3) is connected with the double-station adsorption assembly, and the double-station adsorption assembly is connected with the exhaust assembly;
The exhaust assembly includes a nitrogen exhaust assembly and a control valve E (10).
2. The device for recycling and concentrating the polluted and waste argon discharged from the cold box in the argon recycling process according to claim 1, wherein the pressurizing assembly comprises a pressurizing device (1) and a control valve group H (2), an air inlet end of the pressurizing device (1) is communicated with an external mixed gas supply end, an air inlet end and an air outlet end of the pressurizing device (1) are respectively communicated with two ends of the control valve group H (2), and an air outlet end of the pressurizing device (1) is connected with a buffer assembly (3).
3. The device for recycling and concentrating the polluted and waste argon discharged by the argon recycling intercooler tank according to claim 2, wherein the buffer component (3) comprises an air inlet pipe (31), an end cover (32), a mounting seat (33), a tank body (34), an air outlet pipe (35), a sliding groove (36), a mounting tank (37) and a vent hole (38), the air inlet end of the tank body (34) is fixedly connected with the mounting seat (33), the air inlet end of the mounting seat (33) is detachably connected with the end cover (32), the air inlet end of the end cover (32) is fixedly connected with the air inlet pipe (31), the air inlet pipe (31) is communicated with the air outlet end of the supercharging device (1), the air outlet end of the tank body (34) is fixedly connected with the air outlet pipe (35), a plurality of sliding grooves (36) are formed in an inner circumferential array of the tank body (34), the outer end of the mounting tank (37) is embedded into the sliding groove (36) and is in sliding connection with the tank body (34), a plurality of vent holes (38) are formed in two ends of the mounting tank (37), dry silicon rubber particles are filled in the inner part of the mounting tank (37), and the air outlet pipe (35) is communicated with the double-station adsorption component.
4. A cold box discharged dirty waste argon recovery concentrating apparatus according to claim 3, wherein the diameter of the vent hole (38) is smaller than the diameter of the silicon gel particle.
5. The device for recycling and concentrating the polluted and waste argon discharged from the cold box in recycling the argon according to claim 4, wherein a detector for detecting the moisture of the mixed gas is fixedly arranged in the air outlet pipe (35).
6. The apparatus of claim 5, wherein the air inlet end of the mounting base (33) is detachably connected with the tank (34) by screws.
7. The device for recycling and concentrating the polluted and waste argon discharged from the cold box in recycling of argon according to claim 6, wherein a sealing ring is arranged between the end cover (32) and the mounting seat (33).
8. The device for recycling and concentrating the polluted waste argon discharged from the argon recycling intercooler tank according to claim 7, wherein the double-station adsorption assembly comprises a control valve A (4), a first adsorption tower (5), a control valve B (6), a control valve C (7), a second adsorption tower (8) and a control valve D (9), the air outlet end of the control valve A (4) is communicated with the air inlet end of the first adsorption tower (5), the air outlet end of the first adsorption tower (5) is communicated with the air inlet end of the control valve B (6), the air outlet end of the control valve C (7) is communicated with the air inlet end of the second adsorption tower (8), the air outlet end of the second adsorption tower (8) is communicated with the air inlet end of the control valve D (9), the air inlet ends of the first adsorption tower (5) and the second adsorption tower (8) are both connected with the nitrogen gas exhaust assembly, and the air outlet ends of the control valve B (6) and the control valve D (9) are both communicated with the control valve E (10).
9. The device for recycling and concentrating the polluted and waste argon discharged from the argon recycling intercooler tank according to claim 8, wherein the air inlet ends of the control valve A (4) and the control valve C (7) are communicated with the air outlet pipe (35).
10. The device for recycling and concentrating the polluted and waste argon discharged from the cold box in recycling of argon according to claim 9, wherein the nitrogen gas exhaust assembly comprises a control valve F (11), a control valve G (12) and a vacuum pump (13), air inlet ends of the control valve F (11) and the control valve G (12) are respectively communicated with air inlet ends of the first adsorption tower (5) and the second adsorption tower (8), and air outlet ends of the control valve F (11) and the control valve G (12) are respectively communicated with air inlet ends of the vacuum pump (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202323230082.2U CN221156002U (en) | 2023-11-29 | 2023-11-29 | Dirty useless argon gas recovery enrichment facility of argon gas recovery intercooler tank discharge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202323230082.2U CN221156002U (en) | 2023-11-29 | 2023-11-29 | Dirty useless argon gas recovery enrichment facility of argon gas recovery intercooler tank discharge |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221156002U true CN221156002U (en) | 2024-06-18 |
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ID=91440687
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202323230082.2U Active CN221156002U (en) | 2023-11-29 | 2023-11-29 | Dirty useless argon gas recovery enrichment facility of argon gas recovery intercooler tank discharge |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221156002U (en) |
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2023
- 2023-11-29 CN CN202323230082.2U patent/CN221156002U/en active Active
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