Gas-liquid separation device and working method thereof

Abstract

The present application discloses a gas-liquid separation device and a working method thereof, the gas-liquid separation device comprising a shell body, a separation cylinder and at least one floating pressing assembly, the shell body forming a first interface and a second interface, a peripheral wall of a part of the separation cylinder and an inner wall of the shell body forming a flow channel, the separation cylinder having a separation space, the separation cylinder forming a plurality of first openings connecting the flow channel and the separation space, the separation cylinder forming a flow channel, the separation cylinder forming a plurality of second openings connecting the flow channel and the separation space, the material gas enters from any one of the first interface and the second interface in the axial direction of the shell body and flows through the separation cylinder in the radial direction of the shell body and finally flows out from the other one, the floating pressing assembly applies floating pressure to the filler in the separation space, compared with the existing axial flow method, it realizes dispersion of the material gas while ensuring uniform gas-liquid separation time of the material gas, and adapts to the volume change of the filler, improves the gas-liquid separation effect, and prevents the filler from loosening and friction powdering.

Description

Technical Field

[0001] The present invention relates to the technical field of gas-liquid separation equipment, and in particular to gas-liquid separation equipment and a working method thereof. Background Art

[0002] Gas-liquid separation is an important production link in the chemical, food processing, and pharmaceutical industries. When the current gas-liquid separation equipment is in use, the feed gas is mostly separated by axial flow, that is, the feed gas is introduced from one end of the separation cylinder of the gas-liquid separation equipment and impacts the distributor in the separation cylinder, and is dispersed by the distributor. The dispersed feed gas passes through the packing in the separation cylinder and is finally discharged from the other end of the separation cylinder. In this process, the flow rate of the feed gas will be non-uniform after being dispersed by the distributor, which makes the retention time of the feed gas in the packing non-uniform, resulting in poor gas-liquid separation effect.

[0003] In addition, after the packing is loaded into the separation cylinder, it is usually compressed by a fixed compression mechanism. Due to the uneven distribution of the packing, the packing may sink during the gas-liquid separation process. At this time, the fixed compression mechanism loses its compression function, and the packing is loosened by the airflow and partially rubbed against each other to powder, which weakens the gas-liquid separation effect of the packing, resulting in a relatively short service life and low utilization rate of the packing. At the same time, part of the packing is powdered to form a channel flow, causing part of the gas to flow out directly through the channel flow area without gas-liquid separation, resulting in a high water content in the gas after gas-liquid separation, and the gas-liquid separation does not meet the standard. Summary of the invention

[0004] In order to solve the above technical problems and achieve at least one advantage of the present invention, the present invention provides a gas-liquid separation device, the gas-liquid separation device comprising:

[0005] A shell body, wherein upper and lower ends of the shell body respectively form a first interface and a second interface;

[0006] A separation cylinder, wherein the separation cylinder is installed in the shell body and a part of the peripheral wall forms a flow channel with the inner wall of the shell body, the first interface is communicated with the flow channel, the separation cylinder has a separation space, the separation space is used to accommodate fillers, and the peripheral wall of the separation cylinder forming the flow channel forms a plurality of first openings connecting the flow channel and the separation space, the separation cylinder forms a flow channel, the separation space is located outside the flow channel, the flow channel is communicated with the second interface, the peripheral wall of the separation cylinder forming the flow channel forms a plurality of second openings connecting the flow channel and the separation space, and the material gas can enter from either the first interface or the second interface in the axial direction of the shell body and flow through the separation cylinder in the radial direction of the shell body and finally flow out from the other;

[0007] At least one floating pressing assembly is installed at the high end of the separation space, and the floating pressing assembly applies floating pressure to the filler in the separation space.

[0008] According to one embodiment of the present invention, the floating pressure assembly includes a floating pressure member and a connecting member, the floating pressure member is slidably installed at the high end of the separation space, and the floating pressure member is connected to the inner wall of the separation space formed by the separation cylinder through the connecting member, the floating pressure member can be lifted up by the filler in the separation space and pull the connecting member, the floating pressure member can slide down under its own gravity to compress the filler in the separation space, the connecting member is implemented as a wire mesh, the wire mesh is installed at the bottom of the floating pressure member and its two ends extend downward at intervals to be respectively connected to the two opposite inner walls of the separation space, the wire mesh can confine the filler below the floating pressure member.

[0009] According to one embodiment of the present invention, the separation cylinder includes a separation body and at least one partition, the separation space, the first port, the flow channel and the second port are all formed on the separation body, at least one partition extends upward from the bottom wall forming the separation space and divides the separation space into at least two separation chambers, the partition has a plurality of connecting holes connecting two adjacent separation chambers, all of the separation chambers are located between the flow channel and the flow channel, one of the separation chambers is connected to the flow channel through the first port, and one of the separation chambers is connected to the flow channel through the second port, and at least two of the separation chambers respectively accommodate different fillers, and at least two of the floating clamping assemblies are provided, and one of the floating clamping assemblies is installed at the high end of each of the separation chambers, and each of the floating clamping assemblies applies floating pressure to the filler in the corresponding separation chamber.

[0010] According to one embodiment of the present invention, one end of the separation cylinder close to the first interface and the inner wall of the shell body together form a diversion chamber that connects the flow channel and the first interface, and the gas-liquid separation equipment also includes a guide member, which is installed in the diversion chamber. The material gas entering the diversion chamber through the first interface can be guided by the guide member to flow toward the flow channel.

[0011] According to one embodiment of the present invention, the gas-liquid separation equipment also includes at least one flow baffle assembly, the flow baffle assembly includes a flow baffle member, the flow baffle member has at least one flow hole, the flow baffle member is installed on the inner wall of the flow channel, and the flow baffle member of the flow baffle assembly is arranged at the lower end of the flow channel.

[0012] According to one embodiment of the present invention, the baffle assembly also includes an adjusting member, the baffle is stacked with the adjusting member, the adjusting member has at least one adjusting hole, the adjusting member is configured to be rotatable to adjust the degree of misalignment between the adjusting hole and the flow hole, so as to adjust the flow rate of the gas after gas-liquid separation passing through the flow hole within a predetermined flow range, thereby adjusting the flow resistance of the gas after gas-liquid separation in the flow channel located below the corresponding baffle. When the adjusting hole corresponds to the flow hole, the flow rate of the gas after gas-liquid separation passing through the flow hole is the maximum flow rate in the predetermined flow range, and the flow resistance of the gas after gas-liquid separation in the flow channel located below the corresponding baffle is the smallest. When the adjusting hole is misaligned with the flow hole and the flow hole is blocked by the adjusting member to a predetermined degree, the flow rate of the gas after gas-liquid separation passing through the flow hole is the minimum flow rate in the predetermined flow range, and the flow resistance of the gas after gas-liquid separation in the flow channel located below the corresponding baffle is the largest.

[0013] According to one embodiment of the present invention, the baffle assembly also includes a driving member, the adjusting member is installed on the driving member and can be driven to rotate by the driving member, and the gas-liquid separation equipment also includes a detection member and a controller, the detection member is installed on one end of the shell body to form the second interface, the detection member is used to detect the water content of the gas after gas-liquid separation flowing through the second interface, the detection member is communicatively connected to the controller, and the driving member is controllably connected to the controller, when the detection member detects that the water content of the gas after gas-liquid separation flowing through the second interface is higher than a predetermined value, and the controller receives feedback from the detection member and controls the operation of the driving member, the driving member drives the adjusting member to rotate to increase the degree of offset between the adjusting hole and the flow hole, so as to reduce the flow rate of the gas after gas-liquid separation passing through the flow hole, and then increase the flow resistance of the gas after gas-liquid separation in the flow channel corresponding to the baffle member, so as to adjust the distribution of the gas guided to the separation cylinder by the flow channel.

[0014] According to one embodiment of the present invention, a plurality of baffle assemblies are provided, and the plurality of baffle assemblies are arranged from the lower end portion to the high end portion of the flow channel. When the detection member detects that the water content of the gas after gas-liquid separation flowing through the second interface is higher than a predetermined value, the controller receives feedback from the detection member and sequentially controls the driving members of the plurality of baffle assemblies from bottom to top to selectively drive the adjusting member to rotate, so as to selectively adjust the flow rate of the gas after gas-liquid separation flowing through each baffle member.

[0015] In order to solve the above technical problems and achieve at least one advantage of the present invention, the present invention provides a gas-liquid separation device, the gas-liquid separation device comprising:

[0016] A shell body, wherein upper and lower ends of the shell body respectively form a first interface and a second interface;

[0017] A separation cylinder, wherein the separation cylinder is installed in the shell body and a part of the peripheral wall forms a flow channel with the inner wall of the shell body, the first interface is communicated with the flow channel, the separation cylinder has a separation space, the separation space is used to accommodate fillers, and the peripheral wall of the separation cylinder forming the flow channel forms a plurality of first openings connecting the flow channel and the separation space, the separation cylinder forms a flow channel, the separation space is located outside the flow channel, the flow channel is communicated with the second interface, the peripheral wall of the separation cylinder forming the flow channel forms a plurality of second openings connecting the flow channel and the separation space, the material gas can be introduced into the flow channel from the first interface and flow into the separation cylinder in the radial direction of the shell body to perform gas-liquid separation in the separation cylinder, and the material gas after gas-liquid separation flows through the flow channel and is discharged through the second interface;

[0018] A detection member, the detection member is installed at one end of the shell body forming the second interface, and the detection member is used to detect the water content of the gas after gas-liquid separation flowing through the second interface;

[0019] A controller, wherein the detection element is communicatively connected to the controller;

[0020] At least one baffle assembly, the baffle assembly comprising:

[0021] A baffle, the baffle having at least one flow hole, the baffle being mounted on the inner wall of the flow channel, and the baffle of the baffle assembly being disposed at a lower end of the flow channel;

[0022] An adjusting member, wherein the baffle member is stacked with the adjusting member, the adjusting member has at least one adjusting hole, and the adjusting member is configured to be rotatable to adjust the degree of misalignment between the adjusting hole and the flow hole, so as to adjust the flow rate of the gas after gas-liquid separation passing through the flow hole within a predetermined flow rate range, thereby adjusting the flow resistance of the gas after gas-liquid separation in the flow channel located below the corresponding baffle member. When the adjusting hole corresponds to the flow hole, the flow rate of the gas after gas-liquid separation passing through the flow hole is the maximum flow rate within the predetermined flow rate range, and the flow resistance of the gas after gas-liquid separation in the flow channel located below the corresponding baffle member is the smallest. When the adjusting hole is misaligned with the flow hole and the flow hole is blocked by the adjusting member to a predetermined degree, the flow rate of the gas after gas-liquid separation passing through the flow hole is the minimum flow rate within the predetermined flow rate range, and the flow resistance of the gas after gas-liquid separation in the flow channel located below the corresponding baffle member is the largest.

[0023] The driving member, the adjusting member is installed on the driving member and can be driven to rotate by the driving member, the driving member is controllably connected to the controller, when the detecting member detects that the water content of the gas after gas-liquid separation flowing through the second interface is higher than a predetermined value, and the controller receives feedback from the detecting member and controls the driving member to operate, the driving member drives the adjusting member to rotate to increase the degree of misalignment between the adjusting hole and the flow hole, so as to reduce the flow rate of the gas after gas-liquid separation passing through the flow hole, and then increase the flow resistance of the gas after gas-liquid separation located below the corresponding baffle member in the flow channel.

[0024] In order to solve the above technical problems and achieve at least one advantage of the present invention, the present invention provides a working method of a gas-liquid separation device, the working method of the gas-liquid separation device comprising the following steps:

[0025] The material gas is introduced into the flow channel from the first interface and flows into the separation cylinder in the radial direction of the shell body to perform gas-liquid separation in the separation cylinder. The material gas after gas-liquid separation is introduced into the flow channel. The material gas after gas-liquid separation flowing in the flow channel passes through the flow hole of the flow baffle member provided in the flow channel and is finally discharged from the second interface.

[0026] The detection component detects the water content of the gas after gas-liquid separation flowing through the second interface. When the detection component detects that the water content is higher than a predetermined value, and the controller receives feedback from the detection component and controls the operation of the driving component, the driving component drives the adjusting component to rotate to increase the degree of misalignment between the adjusting hole and the flow hole, thereby reducing the flow rate of the gas after gas-liquid separation passing through the flow hole, and then increasing the flow resistance of the gas after gas-liquid separation in the flow channel corresponding to the baffle component, thereby adjusting the distribution of the gas introduced into the separation cylinder from the flow channel.

[0027] Compared with the prior art, the gas-liquid separation device of the present invention has the following technical effects:

[0028] 1. The feed gas is introduced from the axial direction of the shell body and the gas-liquid separation is carried out in a radial flow manner. Compared with the existing axial flow method, there is no need to introduce a distributor, which can achieve the dispersion of the feed gas while ensuring the uniformity of the gas-liquid separation time of the feed gas, and the gas-liquid separation effect is better. The resistance of the feed gas when passing through the packing is smaller, and it is more energy-saving to use.

[0029] 2. The feed gas is introduced into the shell body from the axial direction and radial flow is used for gas-liquid separation. Compared with the existing axial flow method, the utilization rate of the filler is higher, which effectively avoids the reduction of filler utilization rate due to the airflow distribution factor causing part of the filler to be unusable, so as to achieve the expected gas-liquid separation effect, save the amount of filler used by improving the utilization rate of the filler, and thus reduce the gas-liquid separation cost.

[0030] 3. The floating pressure component is used to apply floating pressure to the packing in the shell body to adapt to the volume change of the packing, ensure that the packing always remains tight, improve the gas-liquid separation effect, prevent the packing from loosening and friction powdering, extend the service life of the packing, and improve the utilization rate of the packing.

[0031] 4. While the floating pressing member of the floating pressing assembly is used to apply floating pressure to the filler in the shell body, the connecting member implemented as a wire mesh confines the filler under the floating pressing member to prevent the filler from leaking from the gap between the floating pressing member and the inner wall of the shell body.

[0032] 5. By detecting the water content of the feed gas after gas-liquid separation, the vertical distribution of the feed gas before gas-liquid separation is adjusted in real time, so that the feed gas introduced into the separation cylinder is more uniform, thereby ensuring that the feed gas can be evenly processed. Compared with the method of only guiding the axial flow of the feed gas, it is effectively avoided that the feed gas is concentrated at the lower end of the separation cylinder, resulting in poor gas-liquid separation effect, thereby improving the gas-liquid separation effect. BRIEF DESCRIPTION OF THE DRAWINGS

[0033] Figure 1 The schematic diagram of the structure of the gas-liquid separation device of the present invention is shown.

[0034] Figure 2 A structural side view of the gas-liquid separation device of the present invention is shown.

[0035] Figure 3 Shows Figure 2 A magnified view of the local structure.

[0036] Figure 4 A partial structural stereogram of the gas-liquid separation device of the present invention is shown.

[0037] Figure 5 Shows Figure 4 A magnified view of the local structure.

[0038] Reference numerals:

[0039] Flow channel 1001; diversion cavity 1002;

[0040] Shell body 10; first interface 101; second interface 102; housing 11; operation port 1101; closure member 12;

[0041] Separation cylinder 20; separation space 201; separation chamber 2011; first opening 202; flow channel 203; second opening 204; separation body 21; partition 22; communication hole 2201;

[0042] Floating pressing assembly 30; floating pressing member 31; pressing body 311; material opening 31101; counterweight body 312; connecting member 32;

[0043] A flow guide 40;

[0044] Flow blocking assembly 50; flow blocking member 51; flow hole 5101; adjustment member 52; adjustment hole 5201; driving member 53;

[0045] Detection piece 60;

[0046] Controller 70. DETAILED DESCRIPTION

[0047] The following description is used to disclose the present invention so that those skilled in the art can implement the present invention. The preferred embodiments described below are only examples, and those skilled in the art can think of other obvious variations. The basic principles of the present invention defined in the following description can be applied to other embodiments, variations, improvements, equivalents, and other technical solutions that do not deviate from the spirit and scope of the present invention.

[0048] Those skilled in the art should understand that, in the disclosure of the present invention, the terms "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside" and the like indicating the orientation or position relationship are based on the orientation or position relationship shown in the drawings, which are only for the convenience of describing the present invention and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operate in a specific orientation. Therefore, the above terms should not be understood as limiting the present invention.

[0049] It is to be understood that the term "one" should be understood as "at least one" or "one or more", that is, in one embodiment, the number of an element may be one, while in another embodiment, the number of the element may be multiple, and the term "one" should not be understood as a limitation on the quantity.

[0050] refer to Figures 1 to 3The gas-liquid separation device according to a preferred embodiment of the present invention will be described in detail below. The gas-liquid separation device includes a shell body 10 and a separation cylinder 20. The upper and lower ends of the shell body 10 respectively form a first interface 101 and a second interface 102. The separation cylinder 20 is installed in the shell body 10 and a part of the peripheral wall forms a flow channel 1001 with the inner wall of the shell body 10. The first interface 101 is connected with the flow channel 1001. The separation cylinder 20 has a separation space 201, and the separation space 201 is used to accommodate fillers. The peripheral wall of the separation cylinder 20 forming the flow channel 1001 forms a plurality of first openings 202 that connect the flow channel 1001 with the separation space 201. The separation cylinder 20 forms a flow channel 203, the separation space 201 is located outside the flow channel 203, the flow channel 203 is connected to the second interface 102, and the peripheral wall of the separation cylinder 20 forming the flow channel 203 forms a plurality of second ports 204 connecting the flow channel 203 and the separation space 201. The material gas can enter from the axial direction of the shell body 10 through any one of the first interface 101 and the second interface 102, and flow through the separation cylinder 20 in the radial direction of the shell body 10 and finally flow out from the other. Compared with the existing axial flow method, there is no need to introduce a distributor, which can achieve the dispersion of the material gas while ensuring the uniform gas-liquid separation time of the material gas, and the gas-liquid separation effect is better, and the resistance of the material gas passing through the filler is smaller, which is more energy-saving.

[0051] In addition, the material gas is separated into gas and liquid by radial flow. Compared with the existing axial flow method, the utilization rate of the filler is higher, which effectively avoids the reduction of filler utilization rate due to the airflow distribution factor causing part of the filler to be unusable. In order to achieve the expected gas-liquid separation effect, the amount of filler used can be saved by improving the utilization rate of the filler, thereby reducing the gas-liquid separation cost.

[0052] It is worth mentioning that the feed gas can be introduced from the first interface 101 into the flow channel 1001 and flow into the separation cylinder 20 from the radial direction of the shell body 10 to perform gas-liquid separation in the separation cylinder 20. After the gas-liquid separation, the feed gas flows through the flow channel 203 and is discharged through the second interface 102, that is, the feed gas flows from the outside to the center; the feed gas can also be introduced from the second interface 102 into the flow channel 203 and flow into the separation cylinder 20 from the radial direction of the shell body 10 to perform gas-liquid separation in the separation cylinder 20. After the gas-liquid separation, the feed gas flows through the flow channel 1001 and is discharged through the first interface 101, that is, the feed gas flows from the center to the outside. In this way, the installation method of the gas-liquid separation equipment is flexible, and the flow direction of the feed gas can be adjusted according to actual needs.

[0053] refer to Figures 2 to 3The gas-liquid separation device further includes at least one floating pressing assembly 30, which is installed at the high end of the separation space 201. The floating pressing assembly 30 applies floating pressure to the packing in the separation space 201 to adapt to the volume change of the packing, ensure that the packing always remains tight, improve the gas-liquid separation effect, prevent the packing from loosening and friction powdering, extend the service life of the packing, and improve the utilization rate of the packing.

[0054] The floating pressing assembly 30 includes a floating pressing member 31 and a connecting member 32. The floating pressing member 31 is slidably mounted at the upper end of the separation space 201, and the floating pressing member 31 is connected to the inner wall of the separation space 201 formed by the separation cylinder 20 through the connecting member 32. The floating pressing member 31 can be lifted up by the filler in the separation space 201 and pull the connecting member 32. The floating pressing member 31 can slide down under its own gravity to compress the filler in the separation space 201, so as to apply floating pressure to the filler.

[0055] Preferably, the connecting member 32 is implemented as a wire mesh, which is installed at the bottom of the floating pressure member 31 and has its two ends extending downward at intervals to be connected to the two opposite inner walls of the separation space 201 respectively. The wire mesh can confine the filler below the floating pressure member 31 to prevent the filler from leaking from the gap between the floating pressure member 31 and the inner wall of the separation space 201.

[0056] As a deformable structure, the connecting member 32 is implemented to include a plurality of springs, which can be elastically deformed when the floating pressing member 31 is lifted by the filler in the separation space 201. The floating pressing member 31 slides down under its own gravity and the elastic force of the spring to compress the filler, ensuring that the filler remains tight.

[0057] Preferably, the floating pressure member 31 includes a pressure body 311 and a counterweight body 312. The pressure body 311 is slidably installed up and down at the high end of the separation space 201, and the counterweight body 312 is installed on the pressure body 311. The counterweight body 312 cooperates with the pressure body 311 to apply floating pressure to the filler in the separation space 201 as a whole.

[0058] It is worth mentioning that the counterweight body 312 is detachably mounted on the pressing body 311 , so that different degrees of pressure can be applied to the filler in the separation space 201 by replacing the counterweight body 312 with different weights.

[0059] refer to Figure 2 and Figure 4The shell body 10 includes a shell 11 and a closure member 12. The first interface 101 and the second interface 102 are both formed in the shell 11. The shell 11 has an operation port 1101 communicating with the interior thereof. The closure member 12 is installed in the shell 11 in a manner that the operation port 1101 can be opened and closed. The operation port 1101 is on the same side as the floating clamping assembly 30, so that the staff can disassemble and assemble the counterweight body 312 to the clamping body 311 through the operation port 1101.

[0060] refer to Figure 5 It is worth mentioning that the pressing body 311 has a material opening 31101, and the counterweight body 312 is detachably mounted on the pressing body 311 in a manner of being inserted into the material opening 31101 and extending toward the separation space 201. When the counterweight body 312 is separated from the pressing body 311, the material opening 31101 is connected to the separation space 201. This allows the staff to remove the counterweight body 312 from the pressing body 311 through the operation opening 1101, and to supplement or replace the filler in the separation space 201 through the material opening 31101.

[0061] refer to Figure 2 Preferably, the separation cylinder 20 comprises a separation body 21 and at least one partition 22, the separation space 201, the first opening 202, the flow channel 203 and the second opening 204 are all formed in the separation body 21, at least one partition 22 extends upward from the bottom wall forming the separation space 201 and divides the separation space 201 into at least two separation chambers 2011, and the partition 22 has a plurality of connecting holes 2201 connecting two adjacent separation chambers 2011. All the separation chambers 2011 are located between the flow channel 1001 and the flow channel 203, wherein one of the separation chambers 2011 is connected to the flow channel 1001 through the first opening 202, and one of the separation chambers 2011 is connected to the flow channel 203 through the second opening 204. At least two of the separation chambers 2011 contain different fillers respectively. At least two floating clamping assemblies 30 are provided, and a floating clamping assembly 30 is installed at the high end of each separation chamber 2011. Each floating clamping assembly 30 applies floating pressure to the filler in the corresponding separation chamber 2011 to meet the needs of compacting fillers with different particle sizes.

[0062] refer to Figure 2The end of the separation cylinder 20 close to the first interface 101 and the inner wall of the shell body 10 form a diversion chamber 1002 that connects the flow channel 1001 and the first interface 101. The gas-liquid separation device also includes a guide member 40, which is installed in the diversion chamber 1002. The material gas entering the diversion chamber 1002 through the first interface 101 can be guided by the guide member 40 to flow to the flow channel 1001 to promote the flow of material gas.

[0063] Preferably, with the direction in which the material gas flows through the first interface 101 and enters the diversion chamber 1002 as a reference, the outer wall of the guide member 40 gradually extends obliquely toward the inner wall of the shell body 10, and the material gas impacting the outer wall of the guide member 40 can be diverted by the guide member 40 and dispersed to the flow channel 1001 to make the material gas evenly distributed.

[0064] refer to Figures 2 to 3 The gas-liquid separation device further comprises at least one baffle assembly 50, the baffle assembly 50 comprises a baffle member 51, the baffle member 51 has at least one flow hole 5101, the baffle member 51 is mounted on the inner wall of the flow channel 203, and the baffle member 51 of the baffle assembly 50 is arranged at the lower end of the flow channel 203. In the process that the material gas is introduced into the flow channel 1001 through the first interface 101 and guided to the separation cylinder 20 by the flow channel 1001, the material gas after gas-liquid separation at the lower end of the flow channel 203 is blocked by the corresponding baffle member 51 and slows down the flow, speeding up the material gas in the flow channel 1001 to flow from its lower end to its higher end and be introduced into the higher end of the separation cylinder 20, so as to increase the uniformity of the material gas distribution in the vertical direction, improve the gas-liquid separation effect, and avoid the situation that the material gas is concentratedly guided to the lower end of the separation cylinder 20, resulting in poor gas-liquid separation effect.

[0065] In one embodiment, the baffle assembly 50 is provided with a plurality of baffles 51, and the baffles 51 of the plurality of baffle assemblies 50 are vertically spaced and distributed in the flow channel 203. The flow rate of the gas after gas-liquid separation flowing through each baffle 51 in the flow channel 203 and directed to the second interface 102 is gradually increased, so that the flow resistance of the gas after gas-liquid separation in the flow channel 203 is gradually reduced, so as to accelerate the flow of the gas from the lower end to the higher end of the flow channel 1001, so that the gas in the flow channel 1001 is uniformly introduced into the separation cylinder 20 in the vertical direction, and the gas can be uniformly processed.

[0066] As a preferred implementation of the previous embodiment, the flow holes 5101 of each of the baffles 51 have the same size, and the number of the flow holes 5101 of the plurality of baffles 51 gradually increases from bottom to top.

[0067] As a variation of the previous embodiment, the number of the flow holes 5101 of each of the flow blocking members 51 is the same, and the sizes of the flow holes 5101 of the plurality of flow blocking members 51 gradually increase from bottom to top.

[0068] Preferably, the baffle assembly 50 also includes an adjusting member 52, the baffle member 51 and the adjusting member 52 are stacked, the adjusting member 52 has at least one adjusting hole 5201, and the adjusting member 52 is configured to be rotatable to adjust the degree of misalignment between the adjusting hole 5201 and the flow hole 5101, so as to adjust the flow rate of the gas after gas-liquid separation passing through the flow hole 5101 within a predetermined flow range, and then adjust the flow resistance of the gas after gas-liquid separation in the flow channel 203 corresponding to the bottom of the baffle member 51, so as to adjust the vertical distribution of the gas in the flow channel 1001 according to actual use requirements, to ensure that the gas can be evenly introduced into the separation cylinder 20 in the vertical direction, thereby improving the dehydration effect.

[0069] Specifically, when the regulating hole 5201 corresponds to the flow hole 5101, the flow rate of the gas after gas-liquid separation through the flow hole 5101 is the maximum flow rate in a predetermined flow range, and the gas after gas-liquid separation in the flow channel 203 located below the corresponding baffle 51 is subject to the smallest flow resistance; when the regulating hole 5201 is misaligned with the flow hole 5101 and the flow hole 5101 is blocked to a predetermined degree by the regulating hole 52, the flow rate of the gas after gas-liquid separation through the flow hole 5101 is the minimum flow rate in a predetermined flow range, and the gas after gas-liquid separation in the flow channel 203 located below the corresponding baffle 51 is subject to the largest flow resistance.

[0070] The baffle assembly 50 further includes a driving member 53 , and the adjusting member 52 is mounted on the driving member 53 and can be driven to rotate by the driving member 53 .

[0071] Preferably, the driving member 53 is implemented as a motor.

[0072] refer to Figure 1The gas-liquid separation device further includes a detection member 60 and a controller 70. The detection member 60 is installed at one end of the shell body 10 forming the second interface 102. The detection member 60 is used to detect the water content of the gas after gas-liquid separation flowing through the second interface 102. The detection member 60 is communicatively connected to the controller 70, and the driving member 53 is controllably connected to the controller 70. When the detection component 60 detects that the water content of the gas after gas-liquid separation flowing through the second interface 102 is higher than a predetermined value, and the controller 70 receives feedback from the detection component 60 and controls the operation of the driving component 53, the driving component 53 drives the adjusting component 52 to rotate to increase the degree of misalignment between the adjusting hole 5201 and the flow hole 5101, so as to reduce the flow rate of the gas after gas-liquid separation passing through the flow hole 5101, and then increase the flow resistance of the gas after gas-liquid separation in the flow channel 203 corresponding to the bottom of the baffle 51, so as to adjust the distribution of the gas guided by the flow channel 1001 to the separation cylinder 20. In this way, by detecting the water content of the feed gas after gas-liquid separation, the vertical distribution of the feed gas before gas-liquid separation can be adjusted in real time, so that the feed gas introduced into the separation cylinder 20 is more uniform, thereby ensuring that the feed gas can be evenly processed. Compared with the method of only guiding the axial flow of the feed gas, it is effectively avoided that the feed gas is concentrated at the lower end of the separation cylinder 20, resulting in poor gas-liquid separation effect, thereby improving the gas-liquid separation effect.

[0073] Preferably, the detection element 60 is implemented as a humidity sensor.

[0074] Preferably, the baffle assembly 50 is provided with a plurality of baffle assemblies, and the plurality of baffle assemblies 50 are arranged from the lower end to the higher end of the flow channel 203. When the detection member 60 detects that the water content of the gas after gas-liquid separation flowing through the second interface 102 is higher than a predetermined value, the controller 70 receives feedback from the detection member 60 and sequentially controls the driving members 53 of the plurality of baffle assemblies 50 from bottom to top to selectively drive the regulating member 52 to rotate, so as to selectively adjust the flow rate of the gas after gas-liquid separation flowing through each baffle assemblies 51, so as to keep the flow rate of the gas after gas-liquid separation within a reasonable range while making the gas in the flow channel 1001 uniformly introduced into the separation cylinder 20 in the vertical direction, so as to improve the gas-liquid separation degree of the gas, ensure that the water content of the gas after gas-liquid separation flowing through the second interface 102 detected by the detection member 60 is lower than a predetermined value, and ensure the gas-liquid separation effect of the gas.

[0075] Specifically, when the detection member 60 detects that the water content of the gas after gas-liquid separation flowing through the second interface 102 is higher than a predetermined value, the controller 70 receives feedback from the detection member 60 to control the driving member 53 of the baffle assembly 50 located at the lower end of the flow channel 203 to operate, and the corresponding adjustment member 52 rotates to increase the offset between the adjustment hole 5201 and the flow hole 5101, so as to reduce the flow rate of the gas after gas-liquid separation flowing through the corresponding baffle member 51, so that the flow channel 203 is not too large. The flow resistance of the gas after gas-liquid separation in the flow channel 1001 corresponding to the lower part of the baffle 51 is increased, which accelerates the flow of the gas in the flow channel 1001 from its lower end to its higher end, improves the uniformity of the gas in the flow channel 1001 introduced into the separation cylinder 20, and thus improves the gas-liquid separation degree of the gas. The detection element 60 continuously detects the water content of the gas after gas-liquid separation flowing through the second interface 102; if the detection element 60 detects that the water content of the gas after gas-liquid separation flowing through the second interface 102 is lower than the preset water content, the detection element 60 detects that the water content of the gas after gas-liquid separation flowing through the second interface 102 is lower than the preset water content. When the detection member 60 detects that the water content of the gas after gas-liquid separation flowing through the second interface 102 is still higher than the predetermined value, the controller 70 receives the feedback from the detection member 60 to control the driving member 53 of the baffle assembly 50 located between the lower end and the high end of the flow channel 203 to operate, and the corresponding adjusting member 52 rotates to increase the offset between the adjusting hole 5201 and the flow hole 5101, so as to reduce the amount of gas flowing through the corresponding baffle member 51. The flow rate of the gas after gas-liquid separation increases the flow resistance of the gas after gas-liquid separation located below the corresponding baffle 51 in the flow channel 203, so as to further accelerate the flow of the gas in the flow channel 1001 from its lower end to its higher end, and the detection element 60 continuously detects the water content of the gas after gas-liquid separation flowing through the second interface 102; if the detection element 60 detects that the water content of the gas after gas-liquid separation flowing through the second interface 102 is lower than a predetermined value, the remaining driving elements 53 do not operate;If the detection member 60 detects that the water content of the gas after gas-liquid separation flowing through the second interface 102 is still higher than the predetermined value, the controller 70 receives the feedback from the detection member 60 and controls the driving member 53 of the baffle assembly 50 located at the high end of the flow channel 203 to operate, and the corresponding adjustment member 52 rotates to increase the degree of misalignment between the adjustment hole 5201 and the flow hole 5101, so as to reduce the flow rate of the gas after gas-liquid separation flowing through the corresponding baffle member 51, so that the flow resistance of the gas after gas-liquid separation located below the corresponding baffle member 51 in the flow channel 203 is increased, the flow of the gas in the separation cylinder 20 is slowed down, the gas-liquid separation time of the gas is prolonged, and the gas-liquid separation effect is improved, so as to ensure that the water content of the gas after gas-liquid separation flowing through the second interface 102 meets the standard. ;

[0076] In one embodiment, with reference to the direction in which the material gas is introduced into the shell body 10 from the first opening 202 , the sizes of the first interfaces 101 at different heights gradually increase so that the material gas can flow evenly from the flow channel 1001 to the separation cylinder 20 .

[0077] In another embodiment, with the direction in which the material gas is introduced into the shell body 10 from the first opening 202 as a reference, the first interface 101 formed by the side wall of the separation cylinder 20 forming the flow channel 1001 is gradually denser so that the material gas can flow evenly from the flow channel 1001 to the separation cylinder 20.

[0078] In another embodiment, with the direction in which the material gas is introduced into the shell body 10 from the first opening 202 as a reference, the outer peripheral wall of the separation cylinder 20 gradually extends obliquely toward the inner wall of the shell body 10 to accelerate the flow of the material gas from the lower end of the flow channel 1001 to its high end, so that the material gas can flow evenly to the separation cylinder 20.

[0079] The present application also proposes a working method of the gas-liquid separation device, comprising the following steps:

[0080] The material gas enters the shell body 10 from either the first interface 101 or the second interface 102 in the axial direction, flows through the separation cylinder 20 in the radial direction of the shell body 10, and finally flows out from the other one, so as to separate gas and liquid by the filler compressed by the floating compression assembly 30 in the separation cylinder 20.

[0081] Preferably, the working method of the gas-liquid separation device further comprises the following steps:

[0082] The material gas is introduced into the flow channel 1001 from the first interface 101 and flows into the separation cylinder 20 in the radial direction of the shell body 10 to perform gas-liquid separation in the separation cylinder 20. After the gas-liquid separation, the material gas flows through the flow channel 203 and is discharged through the second interface 102, that is, the material gas flows from the outside to the center; or the material gas is introduced into the flow channel 203 from the second interface 102 and flows into the separation cylinder 20 in the radial direction of the shell body 10 to perform gas-liquid separation in the separation cylinder 20. After the gas-liquid separation, the material gas flows through the flow channel 1001 and is discharged through the first interface 101, that is, the material gas flows from the center to the outside.

[0083] The present application also proposes a working method of the gas-liquid separation device, comprising the following steps:

[0084] The material gas is introduced into the flow channel 1001 from the first interface 101 and flows into the separation cylinder 20 in the radial direction of the shell body 10 to perform gas-liquid separation in the separation cylinder 20. The material gas after gas-liquid separation is introduced into the flow channel 203. The material gas after gas-liquid separation flowing in the flow channel 203 passes through the flow hole 5101 of the baffle 51 provided in the flow channel 203 and is finally discharged from the second interface 102.

[0085] The detection component 60 detects the water content of the gas after gas-liquid separation flowing through the second interface 102. When the detection component 60 detects that the water content is higher than a predetermined value, and the controller 70 receives feedback from the detection component 60 and controls the operation of the driving component 53, the driving component 53 drives the adjusting component 52 to rotate to increase the degree of misalignment between the adjusting hole 5201 and the flow hole 5101, so as to reduce the flow rate of the gas after gas-liquid separation passing through the flow hole 5101, and then increase the flow resistance of the gas after gas-liquid separation in the flow channel 203 corresponding to the baffle 51, so as to adjust the distribution of the gas introduced into the separation cylinder 20 by the flow channel 1001, so that the gas can be evenly introduced into the separation cylinder 20, improve the gas-liquid separation degree of the gas, and ensure that the water content detection of the gas after gas-liquid separation flowing through the second interface 102 meets the standard.

[0086] Preferably, the working method of the gas-liquid separation device further comprises the following steps:

[0087] When the detection member 60 detects that the water content of the gas after gas-liquid separation flowing through the second interface 102 is higher than a predetermined value, the controller 70 receives feedback from the detection member 60 to control the driving member 53 of the baffle assembly 50 located at the lower end of the flow channel 203 to operate, and the corresponding adjusting member 52 rotates to increase the degree of misalignment between the adjusting hole 5201 and the flow hole 5101, so as to reduce the flow rate of the gas after gas-liquid separation flowing through the corresponding baffle member 51, so that the flow resistance of the gas after gas-liquid separation located below the corresponding baffle member 51 in the flow channel 203 is increased, and the gas in the flow channel 1001 is accelerated to flow from its lower end to its higher end, and the uniformity of the gas in the flow channel 1001 introduced into the separation cylinder 20 is improved, thereby improving the gas-liquid separation degree of the gas, and the detection member 60 continuously detects the water content of the gas after gas-liquid separation flowing through the second interface 102;

[0088] If the detection component 60 detects that the water content of the gas after gas-liquid separation flowing through the second interface 102 is lower than the predetermined value, the remaining driving components 53 do not operate; if the detection component 60 detects that the water content of the gas after gas-liquid separation flowing through the second interface 102 is still higher than the predetermined value, the controller 70 receives feedback from the detection component 60 to control the driving component 53 of the baffle assembly 50 located between the lower end and the high end of the flow channel 203 to operate, and the corresponding regulating component 52 rotates. The adjustment hole 5201 is moved to increase the degree of misalignment with the flow hole 5101, so as to reduce the flow rate of the gas after gas-liquid separation flowing through the corresponding baffle 51, so that the flow resistance of the gas after gas-liquid separation located below the corresponding baffle 51 in the flow channel 203 is increased, so as to further accelerate the flow of the gas in the flow channel 1001 from its lower end to its higher end, and the detection component 60 continuously detects the water content of the gas after gas-liquid separation flowing through the second interface 102;

[0089] If the detection component 60 detects that the water content of the gas after gas-liquid separation flowing through the second interface 102 is lower than the predetermined value, the remaining driving components 53 do not operate; if the detection component 60 detects that the water content of the gas after gas-liquid separation flowing through the second interface 102 is still higher than the predetermined value, the controller 70 receives feedback from the detection component 60 to control the driving component 53 of the baffle assembly 50 located at the high end of the flow channel 203 to operate, and the corresponding adjusting component 52 rotates to increase the degree of misalignment between the adjusting hole 5201 and the flow hole 5101, so as to reduce the flow rate of the gas after gas-liquid separation flowing through the corresponding baffle component 51, so that the flow resistance of the gas after gas-liquid separation located below the corresponding baffle component 51 in the flow channel 203 is increased, the flow of the gas in the separation cylinder 20 is slowed down, the gas-liquid separation time of the gas is prolonged, and the gas-liquid separation effect is improved, so as to ensure that the water content detection of the gas after gas-liquid separation flowing through the second interface 102 meets the standard.

[0090] It should be understood by those skilled in the art that the embodiments of the present invention described above and shown in the accompanying drawings are only examples and do not limit the present invention. The advantages of the present invention have been fully and effectively achieved. The functional and structural principles of the present invention have been demonstrated and explained in the embodiments, and the embodiments of the present invention may be deformed or modified in any way without departing from the principles.

Claims

1. Gas-liquid separation equipment, characterized in that: The gas-liquid separation equipment comprises: A shell body, wherein upper and lower ends of the shell body respectively form a first interface and a second interface; A separation cylinder, wherein the separation cylinder is installed in the shell body and a part of the peripheral wall forms a flow channel with the inner wall of the shell body, the first interface is communicated with the flow channel, the separation cylinder has a separation space, the separation space is used to accommodate fillers, and the peripheral wall of the separation cylinder forming the flow channel forms a plurality of first openings connecting the flow channel and the separation space, the separation cylinder forms a flow channel, the separation space is located outside the flow channel, the flow channel is communicated with the second interface, the peripheral wall of the separation cylinder forming the flow channel forms a plurality of second openings connecting the flow channel and the separation space, the material gas can be introduced into the flow channel from the first interface and flow into the separation cylinder in the radial direction of the shell body to perform gas-liquid separation in the separation cylinder, and the material gas after gas-liquid separation flows through the flow channel and is discharged through the second interface; A detection member, the detection member is installed at one end of the shell body forming the second interface, and the detection member is used to detect the water content of the gas after gas-liquid separation flowing through the second interface; a controller, the detection element being communicatively connected to the controller; At least one baffle assembly, the baffle assembly comprising: A baffle, the baffle having at least one flow hole, the baffle being mounted on the inner wall of the flow channel, and the baffle of the baffle assembly being disposed at a lower end of the flow channel; An adjusting member, wherein the baffle member is stacked with the adjusting member, the adjusting member has at least one adjusting hole, and the adjusting member is configured to be rotatable to adjust the degree of misalignment between the adjusting hole and the flow hole, so as to adjust the flow rate of the gas after gas-liquid separation passing through the flow hole within a predetermined flow rate range, thereby adjusting the flow resistance of the gas after gas-liquid separation in the flow channel located below the corresponding baffle member. When the adjusting hole corresponds to the flow hole, the flow rate of the gas after gas-liquid separation passing through the flow hole is the maximum flow rate within the predetermined flow rate range, and the flow resistance of the gas after gas-liquid separation in the flow channel located below the corresponding baffle member is the smallest. When the adjusting hole is misaligned with the flow hole and the flow hole is blocked by the adjusting member to a predetermined degree, the flow rate of the gas after gas-liquid separation passing through the flow hole is the minimum flow rate within the predetermined flow rate range, and the flow resistance of the gas after gas-liquid separation in the flow channel located below the corresponding baffle member is the largest. The driving member, the adjusting member is installed on the driving member and can be driven to rotate by the driving member, the driving member is controllably connected to the controller, when the detecting member detects that the water content of the gas after gas-liquid separation flowing through the second interface is higher than a predetermined value, and the controller receives feedback from the detecting member and controls the driving member to operate, the driving member drives the adjusting member to rotate to increase the degree of misalignment between the adjusting hole and the flow hole, so as to reduce the flow rate of the gas after gas-liquid separation passing through the flow hole, and then increase the flow resistance of the gas after gas-liquid separation located below the corresponding baffle member in the flow channel.

2. The gas-liquid separation device according to claim 1, characterized in that: There are multiple baffle components, and the multiple baffle components are arranged from the lower end to the high end of the flow channel. When the detection component detects that the water content of the gas after gas-liquid separation flowing through the second interface is higher than a predetermined value, the controller receives feedback from the detection component and sequentially controls the driving components of the multiple baffle components from bottom to top to selectively drive the adjusting component to rotate, so as to selectively adjust the flow rate of the gas after gas-liquid separation flowing through each baffle component.

3. The gas-liquid separation device according to claim 2, characterized in that: The gas-liquid separation device comprises at least one floating compression assembly, which is installed at the high end of the separation space and applies floating pressure to the filler in the separation space.

4. The gas-liquid separation device according to claim 3, characterized in that: The floating pressure assembly includes a floating pressure piece and a connecting piece. The floating pressure piece is slidably installed at the high end of the separation space, and the floating pressure piece is connected to the inner wall of the separation space formed by the separation cylinder through the connecting piece. The floating pressure piece can be lifted up by the filler in the separation space and pull the connecting piece. The floating pressure piece can slide down under its own gravity to compress the filler in the separation space. The connecting piece is implemented as a wire mesh, which is installed at the bottom of the floating pressure piece and its two ends extend downward at intervals to be connected to the two opposite inner walls of the separation space respectively. The wire mesh can confine the filler below the floating pressure piece.

5. The gas-liquid separation device according to claim 3 or 4, characterized in that: The separation cylinder includes a separation body and at least one partition, the separation space, the first port, the flow channel and the second port are all formed in the separation body, at least one partition extends upward from the bottom wall forming the separation space and divides the separation space into at least two separation chambers, the partition has a plurality of connecting holes connecting two adjacent separation chambers, all of the separation chambers are located between the flow channel and the flow channel, one of the separation chambers is connected to the flow channel through the first port, and one of the separation chambers is connected to the flow channel through the second port, and at least two of the separation chambers respectively accommodate different fillers, and at least two of the floating clamping assemblies are provided, and a floating clamping assembly is installed at the high end of each of the separation chambers, and each of the floating clamping assemblies applies floating pressure to the filler in the corresponding separation chamber.

6. The gas-liquid separation device according to claim 1, characterized in that: One end of the separation cylinder close to the first interface and the inner wall of the shell body together form a diversion chamber that connects the flow channel and the first interface. The gas-liquid separation equipment also includes a guide member, which is installed in the diversion chamber. The material gas entering the diversion chamber through the first interface can be guided by the guide member to flow toward the flow channel.

7. A working method of the gas-liquid separation device according to any one of claims 1 to 6, characterized in that: The working method of the gas-liquid separation device comprises the following steps: The material gas is introduced into the flow channel from the first interface and flows into the separation cylinder in the radial direction of the shell body to perform gas-liquid separation in the separation cylinder. The material gas after gas-liquid separation is introduced into the flow channel. The material gas after gas-liquid separation flowing in the flow channel passes through the flow hole of the flow baffle member provided in the flow channel and is finally discharged from the second interface. The detection component detects the water content of the gas after gas-liquid separation flowing through the second interface. When the detection component detects that the water content is higher than a predetermined value, and the controller receives feedback from the detection component and controls the operation of the driving component, the driving component drives the adjusting component to rotate to increase the degree of misalignment between the adjusting hole and the flow hole, thereby reducing the flow rate of the gas after gas-liquid separation passing through the flow hole, and then increasing the flow resistance of the gas after gas-liquid separation in the flow channel corresponding to the baffle component, thereby adjusting the distribution of the gas introduced into the separation cylinder from the flow channel.

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