Automatic mixed gas separating, condensing and trapping device for vacuumizing
By setting up a cyclone separator and condensation reservoir at the exhaust end of the vacuum equipment, dust filtration and chemical condensation capture are realized, which solves the problem of blockage and jamming of vacuum equipment when dealing with dust and gas-liquid media, ensuring the stability of the equipment Operate and achieve energy conservation and emission reduction.
Patent Information
- Application Number
- CN202323404324.5
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2023-12-14
- Publication Date
- 2024-12-20
- Estimated Expiration
- 2033-12-14
AI Technical Summary
Existing vacuum equipment is prone to clogging and jamming when dealing with dust and gas-liquid mixed media, and lacks suitable vacuum dust, gas-liquid separation, condensation and automatic separation and capture devices, which affects the normal operation of the equipment.
A mixed gas automatic separation condensation and capture device is designed, including a cyclone separator and a condensation reservoir. The dust is filtered through a cyclone separator and condensed and capture condensable chemicals in the condensation reservoir to realize online Automatic discharge of liquid to prevent dust and liquid from entering the vacuum equipment.
Effectively prevent dust from entering the vacuum system, reduce harmful emissions, ensure long-term and stable operation of the vacuum system, and achieve energy conservation, emission reduction and economic benefits.
Smart Images

Figure CN222196394U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of vacuum application, in particular to an automatic separation, condensation and collection device for mixed gas used for vacuuming. Background Art
[0002] In the past three decades, the national economy has developed by leaps and bounds, and the vacuum industry is no exception. Various special and complex gases in industrial production need to be vacuumed, especially in the chemical, pharmaceutical, new materials, new energy and other industries, which have higher and higher requirements for vacuum technology. Vacuum equipment has been widely used in all walks of life, especially in recent years, it has played an important role in new materials chemical industry, innovative drug production, power lithium battery, polysilicon solar energy and other industries. Because there are a lot of dust and condensable and non-condensable chemicals in the processes of vacuum concentration, vacuum polymerization reaction, vacuum distillation, vacuum drying and other processes in the above industries, which need to be handled by the vacuum system, once dust and chemical materials enter the vacuum equipment, it will affect the normal operation of the vacuum equipment.
[0003] Since vacuum equipment has high mechanical precision and small clearances between moving parts, it is usually only suitable for pumping clean and dry gas media, and is very sensitive to dust and gas-liquid mixed media. Once a large amount of dust and liquid enter the vacuum equipment, it will cause the vacuum equipment to have an increased load and temperature rise. In severe cases, the vacuum equipment may become blocked or stuck. Currently, there is no dust, gas-liquid separation, condensation, and automatic separation, capture, and discharge device suitable for vacuum equipment. In order to meet the needs of many emerging industries for special gas vacuuming, there is an urgent need for an automatic separation, condensation, and capture device for mixed gases used in vacuuming. Summary of the invention
[0004] The purpose of the utility model is to overcome the above-mentioned shortcomings and provide a mixed gas automatic separation, condensation and capture device for vacuuming, which can filter the dust of the pumped gas and separate and capture the condensate and dust of the condensable chemical gas in front of the vacuum equipment's exhaust end and realize the function of online automatic liquid drainage, so as to realize the long-term reliable operation of the vacuum equipment and achieve energy saving and emission reduction to improve the economic benefits for users.
[0005] The purpose of the utility model is achieved in this way:
[0006] A mixed gas automatic separation condensation capture device for vacuuming, comprising a cyclone separator, a condensation liquid reservoir and a connecting pipeline, wherein the cyclone separator is connected to the condensation liquid reservoir through the connecting pipeline, and the condensation liquid reservoir is connected to the air extraction end of the vacuum system;
[0007] The cyclone separator comprises a separator cylinder, the top of the separator cylinder is provided with an openable head cover, the bottom of the separator cylinder is a semi-elliptical head cover; the upper part of the separator cylinder is provided with a circular guide ring, and a stainless steel filter element is provided in the guide ring; the top side wall of the separator cylinder is provided with an air inlet A, the lowest position of the bottom of the separator cylinder is provided with a sewage outlet, and the top surface of the head cover is provided with an air outlet A;
[0008] The condensing liquid reservoir comprises a liquid reservoir cylinder, a detachable head cover is provided on the top of the liquid reservoir cylinder, a horizontal middle partition is provided in the liquid reservoir cylinder, the middle partition divides the liquid reservoir cylinder into two upper and lower chambers, the upper part of the liquid reservoir cylinder is a condensing chamber, and the lower chamber is a liquid storage chamber, a liquid outlet pipe is provided between the condensing chamber and the liquid storage chamber, the liquid outlet pipe is arranged on the outer wall of the liquid reservoir cylinder, one end of the liquid outlet pipe is connected to the condensing chamber, and the other end is connected to the liquid storage chamber; a cooling water inlet and a cooling water outlet are provided on the top of the head cover, a spiral cooling coil is provided in the condensing chamber, one end of the cooling coil is connected to the cooling water inlet, and the other end is connected to the cooling water outlet; an air inlet B is provided on one side of the condensing chamber, and an air outlet B is provided on the other side, and a drain port is provided at the lowest position of the bottom of the liquid storage chamber;
[0009] One end of the connecting pipeline is connected to the air outlet A of the cyclone separator, and the other end is connected to the air inlet B of the condensate reservoir, and the air outlet B of the condensate reservoir is connected to the vacuum system.
[0010] Preferably, a level transmitter is provided on the bottom side wall of the separator cylinder.
[0011] Preferably, an automatic sewage valve is provided on the outer side of the sewage outlet.
[0012] Preferably, a stop valve is provided on the liquid outlet pipe.
[0013] Preferably, the middle partition is arranged in the middle of the liquid storage cylinder, and the middle partition is inclined at an angle of 5 to 10 degrees to facilitate liquid discharge.
[0014] Preferably, a vent valve is provided on one side of the liquid storage chamber.
[0015] Preferably, a liquid level transmitter is provided on the bottom side wall of the liquid storage chamber.
[0016] Preferably, an automatic drain valve is provided on the outer side of the drain port.
[0017] Compared with the prior art, the beneficial effects of the utility model are:
[0018] The utility model provides an automatic separation, condensation and capture device for mixed gas used for vacuuming. A cyclone separator and a condensation liquid storage device are arranged in front of the vacuum end of the vacuum equipment to filter dust from the pumped gas and separate and capture condensate and dust from condensable chemical gases and realize the function of online automatic liquid drainage. The utility model ensures the long-term stable and reliable operation of the vacuum system and production equipment.
[0019] The advantages of applying the utility model to the vacuum system are: first, it can prevent dust and other particulate materials of the processing medium from entering the vacuum system; second, chemical materials are condensed and captured before entering the vacuum equipment, which can reduce the emission of harmful substances, and the condensed chemicals can be reused or sold as products, which can achieve increased production, energy saving, emission reduction and environmental protection. BRIEF DESCRIPTION OF THE DRAWINGS
[0020] Figure 1 It is a structural schematic diagram of the utility model.
[0021] in:
[0022] Cyclone separator 1, separator cylinder 11, head cover 12, guide ring 13, stainless steel filter element 14, level transmitter 15, air inlet A16, air outlet A17, drain outlet 18, drain valve 19, condensate reservoir 2, reservoir cylinder 21, head cover 22, middle partition 23, cooling coil 24, cooling water inlet 25, cooling water outlet 26, air inlet B27, air outlet B28, piercing valve 29, stop valve 210, liquid outlet pipe 211, drain outlet 212, drain valve 213, liquid level transmitter 214, connecting pipeline 3, vacuum system 4. Implementation
[0023] In order to better understand the technical solution of the present invention, the following will be described in detail in conjunction with the relevant illustrations. It should be understood that the following specific embodiments are not intended to limit the specific implementation of the technical solution of the present invention, and are only implementations that can be adopted by the technical solution of the present invention. It should be noted that the description of the positional relationship of each component in this article, such as component A being located above component B, is based on the description of the relative positions of the components in the illustration, and is not intended to limit the actual positional relationship of the components. Example 1
[0024] See also Figure 1 , Figure 1 A structural schematic diagram of the utility model is drawn. As shown in the figure, a mixed gas automatic separation condensation capture device for vacuuming comprises a cyclone separator 1, a condensation liquid reservoir 2 and a connecting pipeline 3, wherein the cyclone separator 1 is connected to the condensation liquid reservoir 2 via the connecting pipeline 3, and the condensation liquid reservoir 2 is connected to the exhaust end of the vacuum system 4.
[0025] The cyclone separator 1 comprises a separator cylinder 11, the top of the separator cylinder 11 is provided with an openable head cover 12, and the bottom of the separator cylinder 11 is a semi-elliptical head; the upper part of the separator cylinder 11 is provided with a circular guide ring 13, and a 100-mesh stainless steel filter element 14 is provided in the guide ring 13, and a level transmitter 15 is provided on the bottom side wall of the separator cylinder 11;
[0026] An air inlet A16 is provided on the top side wall of the separator cylinder 11, a sewage outlet 18 is provided at the lowest position of the bottom of the separator cylinder 11, and an automatic sewage valve 19 is provided outside the sewage outlet 18; an air outlet A17 is provided at the center of the top surface of the head cover 12.
[0027] The condensing liquid reservoir 2 comprises a liquid reservoir cylinder 21, a detachable head cover plate 22 is provided on the top of the liquid reservoir cylinder 21, a horizontally placed middle partition plate 23 is provided in the liquid reservoir cylinder 21, the middle partition plate 23 is arranged in the middle of the liquid reservoir cylinder 21, and the middle partition plate 23 is inclined at an angle of 5-10° to facilitate liquid discharge;
[0028] The middle partition 23 divides the liquid reservoir cylinder 21 into two upper and lower chambers. The upper part of the liquid reservoir cylinder 21 is a condensation chamber, and the lower chamber is a liquid storage chamber. A liquid outlet pipe 211 is provided between the condensation chamber and the liquid storage chamber. The liquid outlet pipe 211 is provided on the outer wall of the liquid reservoir cylinder 21. One end of the liquid outlet pipe 211 is connected to the condensation chamber, and the other end is connected to the liquid storage chamber. A stop valve 210 is provided on the liquid outlet pipe 211.
[0029] A cooling water inlet 25 and a cooling water outlet 26 are provided on the top of the head cover plate 22. A spiral cooling coil 24 is provided in the condensation chamber. One end of the cooling coil 24 is connected to the cooling water inlet 25, and the other end is connected to the cooling water outlet 26. An air inlet B27 is provided on one side of the condensation chamber, and an air outlet B28 is provided on the other side.
[0030] A vent valve 29 is provided on one side of the liquid storage chamber, and a liquid level transmitter 214 is provided on the bottom side wall of the liquid storage chamber; a liquid discharge port 212 is provided at the lowest position of the bottom of the liquid storage chamber, and an automatic liquid discharge valve 213 is provided outside the liquid discharge port 212.
[0031] One end of the connecting pipe 3 is connected to the air outlet A17 of the cyclone separator 1 , and the other end is connected to the air inlet B27 of the condensate storage tank 2 . The air outlet B28 of the condensate storage tank 2 is connected to the vacuum system 4 .
[0032] Working principle:
[0033] The high-speed mixed gas enters the separator from the air inlet of the separator, and the mixed gas makes a spiral motion from top to bottom in the annular compartment ring between the guide ring and the inner wall of the separator. Since the cross-sectional area of the compartment ring is much larger than the diameter of the inlet pipe channel, the flow rate of the mixed gas suddenly drops after entering the separator. The large particles of dust and suspended droplets in the mixed gas settle to the bottom of the reservoir along the inner wall of the separator through cyclone separation under the action of centrifugal force and gravity. The remaining gas and micro dust particles continue to flow along the internal channel of the guide ring to the condensation storage tank behind. The micro dust particles in the gas are filtered and separated again in the stainless steel filter element inside the guide ring. Finally, only a small amount of finer dust and gas flow to the rear condensation storage tank through the connecting pipe between the two devices. When the dust or condensate in the separator reaches a certain height, the level sensor will give a signal to the control system, and the dust or condensate is discharged through the drain valve automatically and manually.
[0034] The condensate collector is arranged at the rear stage of the cyclone separator, and the two are connected by a vacuum pipeline.
[0035] After the mixed gas enters the condensation chamber at the top of the trap, it exchanges heat with the cooling water in the cooling coil. Most of the condensable chemicals in the gas are condensed into liquid. Under the action of gravity, the condensate settles to the bottom of the condensation chamber, and then enters the lower chamber of the condensate trap through the condensate collection pipeline. A liquid level transmitter is installed on the lower side of the condensate trap. When the liquid level in the trap reaches the set height, the PLC vacuum system can automatically close the stop valve on the collection pipeline through the model of the liquid level transmitter, isolate the upper and lower chambers, and break the vacuum of the collection tank at the same time, and then open the automatic drain valve at the bottom of the collection tank. When the liquid level reaches the lowest level, the liquid level transmitter sends a signal to the vacuum system, and the system automatically closes the drain valve and the break valve and automatically opens the stop valve on the condensate collection pipeline.
[0036] The above are only specific application examples of the utility model, and do not constitute any limitation on the protection scope of the utility model. Any technical solution formed by equivalent transformation or equivalent replacement falls within the protection scope of the utility model.
Claims
1. A mixed gas automatic separation and condensation trapping device for vacuuming, characterized in that: It comprises a cyclone separator (1), a condensate storage tank (2) and a connecting pipeline (3), wherein the cyclone separator (1) is connected to the condensate storage tank (2) via the connecting pipeline (3), and the condensate storage tank (2) is connected to the air extraction end of a vacuum system (4); The cyclone separator (1) comprises a separator cylinder (11), the top of the separator cylinder (11) is provided with an openable head cover (12), and the bottom of the separator cylinder (11) is a semi-elliptical head cover; a circular guide ring (13) is provided on the upper part of the separator cylinder (11), and a stainless steel filter element (14) is provided in the guide ring (13); an air inlet A (16) is provided on the top side wall of the separator cylinder (11), a sewage outlet (18) is provided at the lowest position of the bottom of the separator cylinder (11), and an air outlet A (17) is provided on the top surface of the head cover (12); The condensing liquid storage tank (2) comprises a liquid storage tank cylinder (21), a detachable head cover plate (22) is provided on the top of the liquid storage tank cylinder (21), a horizontally placed middle partition plate (23) is provided inside the liquid storage tank cylinder (21), and the middle partition plate (23) divides the liquid storage tank cylinder (21) into two upper and lower chambers, the upper part of the liquid storage tank cylinder (21) is a condensing chamber, and the lower chamber is a liquid storage chamber, and a liquid outlet pipe (211) is provided between the condensing chamber and the liquid storage chamber, and the liquid outlet pipe (211) is provided at the liquid storage tank cylinder (21). The outer wall of the condensation chamber has one end of a liquid outlet pipe (211) connected to the condensation chamber, and the other end connected to the liquid storage chamber; a cooling water inlet (25) and a cooling water outlet (26) are provided on the top of the head cover plate (22); a spiral cooling coil (24) is provided in the condensation chamber, one end of the cooling coil (24) is connected to the cooling water inlet (25), and the other end is connected to the cooling water outlet (26); an air inlet B (27) is provided on one side of the condensation chamber, and an air outlet B (28) is provided on the other side; a liquid discharge port (212) is provided at the lowest position of the bottom of the liquid storage chamber; One end of the connecting pipeline (3) is connected to the air outlet A (17) of the cyclone separator (1), and the other end is connected to the air inlet B (27) of the condensate storage tank (2), and the air outlet B (28) of the condensate storage tank (2) is connected to the vacuum system (4).
2. The automatic separation and condensation trapping device for vacuuming mixed gas according to claim 1, characterized in that: A level transmitter (15) is provided on the bottom side wall of the separator cylinder (11).
3. The automatic separation and condensation trapping device for vacuuming mixed gas according to claim 1, characterized in that: An automatic sewage discharge valve (19) is provided on the outer side of the sewage discharge port (18).
4. The automatic separation and condensation trapping device for vacuuming mixed gas according to claim 1, characterized in that: The liquid outlet pipe (211) is provided with a stop valve (210).
5. The automatic separation and condensation trapping device for vacuuming mixed gas according to claim 1, characterized in that: The middle partition (23) is arranged in the middle of the liquid storage cylinder (21), and the middle partition (23) is arranged to be inclined at an angle of 5 to 10 degrees, so as to facilitate liquid discharge.
6. The automatic separation and condensation trapping device for vacuuming mixed gas according to claim 1, characterized in that: A vent valve (29) is provided on one side of the liquid storage chamber.
7. The automatic separation and condensation trapping device for vacuuming mixed gas according to claim 1, characterized in that: A liquid level transmitter (214) is provided on the bottom side wall of the liquid storage chamber.
8. The automatic separation and condensation trapping device for vacuuming mixed gas according to claim 1, characterized in that: An automatic liquid discharge valve (213) is provided on the outer side of the liquid discharge port (212).
