Coalescence-separation ware of filter core can reverse washing in desulfurization sled
Technical Field
The utility model relates to a desulfurization technical field specifically is a coalescence-separation ware of reverse cleaning filter core in desulfurization sled.
Background
Desulfurization, broadly referred to as desulfurization prior to combustion, refers to the removal of sulfur from fuel and prior to the emission of flue gases. Is one of the important technical measures for preventing and controlling the air pollution. When the natural gas is carried, needs get rid of granule impurity and moisture, and this just needs use the desulfurization sled, and traditional desulfurization sled is when using, and inside filter core needs to be dismantled and wash to avoid the filter core to block up, inconvenient washing, simultaneously, to the processing of natural gas not thorough, the internal miscible of natural gas has steam and granule impurity, can't satisfy the demand.
SUMMERY OF THE UTILITY MODEL
The utility model provides a but coalescence-separation ware of reverse cleaning filter core in desulfurization sled, the medium is at first from inside to outside flowing through the coalescence-filter core, this filter core has special filtration, the dual efficiency of coalescence moisture, the separation filter core has good hydrophobic performance, only let the medium pass through, little drop is intercepted outside the filter core completely effectively, and the coalescence becomes big drop and subsides, thereby further separate moisture, ensure effectively to deviate from moisture, and simultaneously, also can realize the effect of reverse cleaning filter core.
In order to achieve the above purpose, the utility model discloses a following technical scheme realizes: the utility model provides a can reverse coalescence separator who washs filter core in desulfurization sled, includes the casing, the top of casing is passed through the bolt fastening and is had the upper cover, there are coalescence filter core and separation filter core through the bolt fastening in the casing, the both sides of casing are close to the bottom intercommunication and are provided with air inlet and gas outlet, air inlet and coalescence filter core intercommunication, gas outlet and separation filter core intercommunication, the liquid trap has been seted up to the position between coalescence filter core and the separation filter core in the casing, the top welding of casing has the drain pipe of liquid trap intercommunication, be provided with two-way solenoid valve on the drain pipe, and the drain pipe is provided with the blow off pipe through two-way.
In order to open the upper cover conveniently, as the utility model relates to a can reverse the coalescence-separation ware of wasing the filter core in the desulfurization sled is preferred, one side welding of casing has hoisting device, and hoisting device's output shaft and upper cover welding.
In order to realize opening the pipeline, conduct the utility model relates to a but the coalescence-separation ware of reverse cleaning filter core is preferred in desulfurization sled, one side intercommunication of casing is provided with the pipeline, and pipeline and blow off pipe intercommunication to be provided with one-way solenoid valve on the pipeline.
In order to conveniently confirm the atmospheric pressure difference of air inlet and gas outlet, as the utility model relates to a but the coalescence-separation ware of reverse cleaning filter core is preferred in desulfurization sled, the front of casing is passed through the bolt fastening and is had the differential pressure gauge, the intercommunication is provided with two pressure differential pipes on the differential pressure gauge, and two pressure differential pipes communicate with air inlet and gas outlet respectively.
In order to observe the position liquid in the casing, as the utility model relates to a but the coalescence-separation ware of reverse cleaning filter core is preferred in the desulfurization sled, the front of casing is fixed with the position liquid meter through the bolt.
In order to avoid the casing internal gas pressure too high, promote the security, conduct the utility model relates to a but the coalescence-separation ware of reverse cleaning filter core is preferred in the desulfurization sled, the casing is provided with the sealing washer with the laminating department of upper cover, and the top of upper cover has seted up safe valve port.
The utility model provides a coalescence-separation device capable of reversely cleaning a filter element in a desulfurization pry. The method has the following beneficial effects:
(1) the utility model discloses a desulfurization sled, but the coalescence separator of reverse cleaning filter core in this desulfurization sled, the liquefied natural gas at first gets into the casing from the air inlet, then flow through the coalescence filter core, the coalescence filter core has the dual function of filtering impurity, the particulate impurity in the coalescence liquid composition, the great liquid droplet of size is gathered to the droplet in the material, the liquid droplet after the coalescence descends to the catch basin under the effect of gravity, the separation filter core has good hydrophobic performance, when the medium is from outside-in when flowing through the separation filter core, only let the medium pass through, the globule is intercepted outside the separation filter core completely effectively, and the coalescence becomes the major globule and subsides, thereby further separate moisture, ensure effectively to deviate from moisture.
(2) The coalescence separator of filter core can reverse washing in this desulfurization sled, and the user can send into the washing water by the drain pipe, washs coalescence filter core and separation filter core, enters into the blow off pipe by the pipeline again, has realized the effect of reverse washing filter core.
Drawings
FIG. 1 is a schematic view of the present invention;
FIG. 2 is a schematic view of the interior of the housing of the present invention;
fig. 3 is a schematic view of the coalescing filter element of the present invention.
In the figure: 1. a housing; 2. an air inlet; 3. an air outlet; 4. an upper cover; 5. a safety valve port; 6. a differential pressure gauge; 7. a lifting device; 8. a differential pressure tube; 9. a level gauge; 10. a drain pipe; 11. a blow-off pipe; 12. a two-way solenoid valve; 13. a pipeline; 14. a one-way solenoid valve; 15. a coalescing filter element; 16. separating the filter element; 17. a liquid collecting tank.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments.
Examples of which are illustrated in the accompanying drawings, wherein like reference numerals refer to the same or similar elements or elements having the same or similar function throughout. The embodiments described below with reference to the drawings are exemplary and intended to be used for explaining the present invention, and should not be construed as limiting the present invention.
Referring to fig. 1-3, the present invention provides a technical solution: the utility model provides a but coalescence-separation ware of reverse cleaning filter core in desulfurization sled, which comprises a housin 1, there is upper cover 4 at casing 1's top through the bolt fastening, there are coalescence filter core 15 and separation filter core 16 through the bolt fastening in casing 1, casing 1's both sides are close to the bottom intercommunication and are provided with air inlet 2 and gas outlet 3, air inlet 2 and 15 intercommunications of coalescence filter core, gas outlet 3 and separation filter core 16 intercommunication, it has seted up collecting tank 17 to lie in between coalescence filter core 15 and the separation filter core 16 in the casing 1, casing 1's top welding has the drain pipe 10 of collecting tank 17 intercommunication, be provided with two-way solenoid valve 12 on the drain pipe 10, and drain pipe 10 is provided with blow off pipe 11 through.
In this embodiment: the natural gas liquid firstly enters the shell 1 from the gas inlet 2 and then flows through the coalescence filter element 15, the coalescence filter element 15 has double functions of impurity filtering and liquid component coalescence, particle impurities in the natural gas are filtered, small liquid drops in the material are gathered into liquid drops with larger size, the gathered liquid drops are descended to the liquid collecting tank 17 under the action of gravity, the separation filter element 16 has good hydrophobic performance, when the medium flows through the separation filter element 16 from outside to inside, only the medium is allowed to pass, small water drops are completely and effectively intercepted outside the separation filter element 16 and are gathered into large water drops to subside, therefore, the moisture is further separated, and the moisture is effectively removed.
Specifically, a lifting device 7 is welded to one side of the housing 1, and an output shaft of the lifting device 7 is welded to the upper cover 4.
In this embodiment: the user can detach the bolt fixing the upper cover 4 and realize the separation of the housing 1 and the upper cover 4 by the lifting device 7, namely, open the upper cover 4.
Specifically, a pipeline 13 is arranged on one side of the shell 1 in a communicating manner, the pipeline 13 is communicated with the sewage draining pipe 11, and a one-way electromagnetic valve 14 is arranged on the pipeline 13.
In this embodiment: the conduction of the pipeline 13 is realized through the arranged one-way electromagnetic valve 14.
Specifically, a differential pressure gauge 6 is fixed on the front surface of the shell 1 through a bolt, two differential pressure pipes 8 are communicated with the differential pressure gauge 6, and the two differential pressure pipes 8 are respectively communicated with the air inlet 2 and the air outlet 3.
In this embodiment: a differential pressure gauge 6 is provided to enable measurement of the difference in air pressure in the inlet 2 and outlet 3.
Specifically, the level gauge 9 is fixed to the front surface of the housing 1 by bolts.
In this embodiment: the level gauge 9 is used to check the depth of the liquid in the housing 1 in real time.
Specifically, a sealing ring is arranged at the joint of the shell 1 and the upper cover 4, and a safety valve port 5 is arranged at the top of the upper cover 4.
In this embodiment: the sealing ring enables the housing 1 and the upper cover 4 to be better fixed in a sealing manner.
When the device is used, liquid natural gas firstly enters the shell 1 from the gas inlet 2 and then flows through the coalescence filter element 15, the coalescence filter element 15 can filter impurities and coalesce liquid components to filter out particle impurities in the natural gas, small droplets in materials are coalesced into droplets with larger size, the coalesced droplets are descended into the liquid collecting tank 17 under the action of gravity, the separation filter element 16 has good hydrophobic performance, when the medium flows through the separation filter element 16 from outside to inside, only the medium passes through, small water droplets are completely and effectively intercepted outside the separation filter element 16 and are coalesced into large water droplets to be subsided, so that the moisture is further separated, the effective moisture removal is ensured, when the coalescence filter element 15 and the separation filter element 16 need to be cleaned, the gas inlet 2 and the gas outlet 3 can be closed, the drain pipe 10 is communicated, the one-way electromagnetic valve 14 is opened, and cleaning water is sent into the drain pipe 10 through an external water, the cleaning water can enter the shell 1 to clean the coalescence filter element 15 and the separation filter element 16, and the cleaned water can enter the sewage discharge pipe 11 through the pipeline 13 to be discharged, so that the effect of reversely cleaning the filter element is realized, and the use is convenient.
The above, only be the concrete implementation of the preferred embodiment of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art is in the technical scope of the present invention, according to the technical solution of the present invention and the utility model, the concept of which is equivalent to replace or change, should be covered within the protection scope of the present invention.