CN216825196U - Dedicated crude benzene oil water separator in coke chemical industry workshop - Google Patents
Dedicated crude benzene oil water separator in coke chemical industry workshop Download PDFInfo
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- CN216825196U CN216825196U CN202220278493.5U CN202220278493U CN216825196U CN 216825196 U CN216825196 U CN 216825196U CN 202220278493 U CN202220278493 U CN 202220278493U CN 216825196 U CN216825196 U CN 216825196U
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Abstract
The utility model discloses a dedicated crude benzol water oil separator in coke chemical product workshop, its structure includes adjustment mechanism and guiding mechanism, through having set up adjustment mechanism inside the separator box, drive negative pressure pipeline and flexible pipeline and the inside air current of negative pressure plate outflow through the negative pressure pump, carry out the primary separation action to oily water through filtering water ring and first oil absorption cotton this moment, and then utilize atmospheric pressure to improve and shunt rivers through water oil separating membrane and second oil absorption cotton, be favorable to improving the effect of taking out of moisture, it makes the inside thermal conductance oil of condensate box get into inside the heat conduction ring board to the water oil of separator box carries out the condensation action through the water conservancy diversion action between heat conduction pump and first electromagnetic directional valve and the second electromagnetic directional valve, thereby make the higher crude benzol oil of crystallization point take place the crystallization and filtered parts such as water ring and carry out the filtration action.
Description
Technical Field
The utility model relates to a coking equipment technical field, concretely relates to dedicated crude benzol oil water separator in coke chemical industry workshop.
Background
In the process of producing and recovering crude benzene purified by coke oven gas in a coking plant, in order to store new wash oil from an oil depot, collect wash oil carried by the gas and discharged from an equipment pipeline, an oil-water separation device is generally arranged, and the wash oil is separated from water by utilizing the principles of different oil-water specific gravity, poor intersolubility and long-time standing, and then is respectively discharged to achieve the purpose of oil-water separation.
At present, chinese patent with publication number CN202021414570.2 discloses an oil-water separator of coking crude benzol emptying oil, and it includes cylinder, liquid distribution pipe and cartridge filter, first apron is installed on the top of cylinder, a plurality of division board is installed to the inside equidistant of cylinder, and all constitutes the cavity of stewing between two adjacent division boards, the one side of the cavity bottom of stewing all communicates there is the honeycomb duct, and the middle part of honeycomb duct all installs the solenoid valve.
The existing oil-water separation device mostly adopts a mechanical oil separation mode, so that the separation effect is poor, oil and water cannot be completely separated, and metal fragments cannot be cleaned by the oil-water separation device, so that the metal fragments remain in the device, the device cannot work, and the separation effect is influenced; meanwhile, most of the existing devices are separated through standing and precipitating or filtering and the like, and the separation method usually needs long working time or has the problem of poor separation effect.
SUMMERY OF THE UTILITY MODEL
Technical problem to be solved
In order to overcome the defects of the prior art, the special crude benzene oil-water separator for the coking production workshop is provided, and the problems that the existing oil-water separation device mostly adopts a mechanical oil separation mode, the separation effect is poor, the oil and water cannot be completely separated, and the oil-water separation device cannot clean metal debris, so that the metal debris remains in the device, the device cannot work and the separation effect is influenced are solved; meanwhile, most of the existing devices are separated through standing precipitation or filtration and other modes, and the mode usually needs long working time or has the problem of poor separation effect.
(II) technical scheme
The utility model discloses a following technical scheme realizes: the utility model provides a dedicated crude benzol water oil separator in coke chemical industry workshop, including separator box, rose box, inlet, adjustment mechanism, water conservancy diversion mechanism, oil extraction pump, sealed maintenance door, control panel, filtering component and storage water tank, separator box top and rose box bottom pipe connection, the rose box left side is equipped with the inlet, separator box top and oil extraction pump bolted connection, separator box front end and sealed maintenance door hinged joint, sealed maintenance door front end and control panel bolted connection, rose box inner wall and filtering component bolted connection, separator box right side bottom and storage water tank bolted connection, the oil extraction pump is connected with the control panel electricity, adjustment mechanism locates the separator box right side, adjustment mechanism includes negative pressure pump, negative pressure pipeline, flexible pipeline, negative pressure board, regulating fluid pole, water filtering ring, The oil-water separation device comprises first oil absorption cotton, a fixed pipeline, an oil-water separation membrane and second oil absorption cotton, wherein the right side of a separation box is connected with a negative pressure pump through bolt, the bottom opening of the negative pressure pump is connected with a top pipeline of a water storage box, the top opening of the negative pressure pump is connected with a negative pressure pipeline, the negative pressure pipeline is connected with a top opening pipeline of a filter box, the negative pressure pipeline is fixedly connected with a circle center through hole of a filter assembly, the negative pressure pipeline is connected with a top pipeline of a telescopic pipeline, the bottom of the telescopic pipeline is connected with a top middle opening pipeline of a negative pressure plate, the left side and the right side of the bottom of the negative pressure plate are both connected with a piston rod of a regulating liquid rod, the regulating liquid rod is fixedly connected with the bottom opening of the separation box, the outer side of the negative pressure plate is connected with an inner annular wall of a water filter ring through bolt, the bottom of the water filter ring is provided with the first oil absorption cotton, the right side of the top of the water filter ring is connected with the bottom of the fixed pipeline, the top of the fixed pipeline is connected with a water inlet pipeline of an oil extraction pump, the inner groove wall of the negative pressure plate is provided with an oil-water separation membrane, the bottom of the inner groove of the negative pressure plate is fixedly connected with a second oil absorption cotton, the negative pressure pump and the liquid regulating rod are electrically connected with the control panel, and the flow guide mechanism is arranged inside the separation box.
Further, the flow guide mechanism comprises a heat conduction ring plate, a first electromagnetic directional valve, a temperature sensor, an electrothermal liquid box, a condensate box, a second electromagnetic directional valve, a heat conduction pump and a return pipe, the inner wall of the separation box is connected with the heat conduction ring plate through a bolt, an opening on the left top side of the heat conduction ring plate is connected with a connecting pipe on the top of the first electromagnetic directional valve through a pipeline, a connecting pipe on the top of the first electromagnetic directional valve is connected with the temperature sensor through a bolt, an opening on the front side of the first electromagnetic directional valve is connected with a pipeline on the top of the electrothermal liquid box, the electrothermal liquid box is connected with a bolt on the left side wall of the separation box, an opening on the rear side of the first electromagnetic directional valve is connected with a pipeline on the top of the condensate box, the condensate box is connected with a bolt on the left side wall of the separation box, openings on the bottoms of the electrothermal liquid box and the condensate box are connected with a water outlet pipeline of the second electromagnetic directional valve, and an opening on the bottom of the second electromagnetic directional valve is connected with a pipeline on the top of the heat conduction pump, the bottom water inlet of the heat-conducting pump is connected with a return pipe pipeline, the return pipe is connected with an opening pipeline at the right bottom side of the heat-conducting annular plate, and the first electromagnetic directional valve, the temperature sensor, the electric heating liquid tank, the condensate liquid tank, the second electromagnetic directional valve and the heat-conducting pump are all electrically connected with the control panel.
Furthermore, the telescopic length of the telescopic pipeline is the same as the adjusting range of the adjusting liquid rod, and the negative pressure plate is parallel to the top in the separation box.
Furthermore, the first oil absorption cotton and the second oil absorption cotton are both oil filter layers with the thickness of 10 cm, and the second oil absorption cotton is parallel to the oil-water separation membrane.
Furthermore, the diameter and the length of the water filtering ring are the same as the diameter of an inner groove of the heat conducting ring plate, and the heat conducting ring plate is in a vertical relation with the inner wall of the water filtering ring.
Furthermore, the first electromagnetic directional valve and the second electromagnetic directional valve are symmetrically distributed, and the thickness of the heat conducting annular plate is 5 cm.
Furthermore, the heat conducting ring plate is made of metal copper.
Furthermore, the material of the return pipe is a heat insulation material.
(III) advantageous effects
Compared with the prior art, the utility model, following beneficial effect has:
1) a dedicated crude benzol water oil separator in coke chemical workshop, through having set up adjustment mechanism inside the separator box, drive negative pressure pipeline and flexible pipeline and the inside air current of negative pressure plate through the negative pressure pump and flow, it carries out the primary separation action to oil water to lead to filtration water ring and first oil absorption cotton this moment, and then utilize atmospheric pressure to improve and shunt water through water oil separating membrane and second oil absorption cotton to rivers, be favorable to improving the effect of taking out of moisture, carry out the displacement regulation action to negative pressure plate and drainage ring through adjusting the liquid pole simultaneously, be favorable to improving the many times filtering separation effect to profit.
2) A dedicated crude benzene oil water separator in coke chemical industry workshop, through having set up water conservancy diversion mechanism inside the separator box, water conservancy diversion between heat conduction pump and first electromagnetic directional valve and the second electromagnetic directional valve is moved and is made the inside thermal conductance oil of condensate box get into inside the heat conduction crown plate, thereby carry out the condensation action to the profit of separator box inside, thereby make the higher crude benzene oil of crystallization point take place the crystallization and filtered the action by parts such as water filtering ring, then after extraction moisture, make its inside thermal conductance oil get into the inside transmission heat of heat conduction crown plate through the water conservancy diversion to the electric heat liquid case, thereby make the crude benzene oil that reaches the crystallization point reply the prefabricate again, be favorable to improving the temperature control effect to water oil separation and play supplementary effect to separation work.
Drawings
Other features, objects and advantages of the invention will become more apparent upon reading of the detailed description of non-limiting embodiments with reference to the following drawings:
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a schematic view of the internal structure of the adjusting mechanism and the separating box of the present invention;
fig. 3 is an enlarged schematic structural view of a point a in fig. 2 according to the present invention;
fig. 4 is a schematic structural view of the flow guide mechanism of the present invention;
fig. 5 is a left side view structural diagram of the diversion mechanism of the present invention.
In the figure: the device comprises a separation tank-1, a filter tank-2, a liquid inlet-3, an adjusting mechanism-4, a flow guide mechanism-5, an oil discharge pump-6, a sealing maintenance door-7, a control panel-8, a filter assembly-9, a water storage tank-10, a negative pressure pump-41, a negative pressure pipeline-42, a telescopic pipeline-43, a negative pressure plate-44, an adjusting liquid rod-45, a water filtering ring-46, a first oil absorption cotton-47, a fixed pipeline-48, an oil-water separation membrane-49, a second oil absorption cotton-410, a heat conduction ring plate-51, a first electromagnetic directional valve-52, a temperature sensor-53, an electric heating liquid tank-54, a condensate tank-55, a second electromagnetic directional valve-56, a heat conduction pump-57 and a return pipe-58.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more clearly understood, the present invention is further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
Referring to fig. 1, the utility model provides a special crude benzene oil water separator for coke chemical workshop: including separator box 1, rose box 2, the inlet 3, adjustment mechanism 4, water conservancy diversion mechanism 5, oil extraction pump 6, sealed maintenance door 7, control panel 8, filtering component 9 and storage water tank 10, 1 top of separator box and 2 bottom pipe connections of rose box, 2 left sides of rose box are equipped with inlet 3, 1 top of separator box and oil extraction pump 6 bolted connection, 1 front end of separator box and 7 hinged joint of sealed maintenance door, 7 front ends of sealed maintenance door and 8 bolted connection of control panel, 2 inner walls of rose box and 9 bolted connection of filtering component, 1 right side bottom of separator box and storage water tank 10 bolted connection, oil extraction pump 6 is connected with 8 electricity of control panel.
Referring to fig. 2 and 3, the utility model provides a special crude benzene oil-water separator for coke chemical production workshop, the adjusting mechanism 4 is arranged on the right side of the separating box 1 to improve the adjusting effect, the adjusting mechanism 4 comprises a negative pressure pump 41, a negative pressure pipeline 42, a telescopic pipeline 43, a negative pressure plate 44, a liquid regulating rod 45, a water filtering ring 46, a first oil-absorbing cotton 47, a fixed pipeline 48, an oil-water separating membrane 49 and a second oil-absorbing cotton 410, the right side of the separating box 1 is connected with the negative pressure pump 41 by bolts to improve the fixing effect of the negative pressure pump 41, the bottom opening of the negative pressure pump 41 is connected with the top pipeline of the water storage tank 10 to improve the flow guiding effect of the negative pressure pump 41, the top opening of the negative pressure pump 41 is connected with the negative pressure pipeline 42 to improve the flow guiding effect of the negative pressure pump 41, the negative pressure pipeline 42 is connected with the top opening pipeline of the filtering box 2 to improve the fixing effect of the negative pressure pipeline 42, the negative pressure pipeline 42 is fixedly connected with the through hole of the center of the filtering component 9, the flow guiding effect of the negative pressure pipeline 42 is improved, the negative pressure pipeline 42 is connected with the top pipeline of the telescopic pipeline 43, the flow guiding effect of the telescopic pipeline 43 is improved, the bottom of the telescopic pipeline 43 is connected with the pipeline with the opening at the middle part of the top of the negative pressure plate 44, the flow guiding effect of the negative pressure plate 44 is improved, the left side and the right side of the bottom of the negative pressure plate 44 are both connected with the piston rod bolt of the regulating liquid rod 45, the adjusting effect of the regulating liquid rod 45 is improved, the regulating liquid rod 45 is fixedly connected with the opening at the bottom of the separation box 1, the fixing effect of the regulating liquid rod 45 is improved, the outer side of the negative pressure plate 44 is connected with the inner ring wall bolt of the water filtering ring 46, the fixing effect of the water filtering ring 46 is improved, the first oil absorbing cotton 47 is arranged at the bottom of the water filtering ring 46, the oil absorbing effect of the first oil absorbing cotton 47 is improved, the right side of the top of the water filtering ring 46 is connected with the bottom of the fixed pipeline 48, the top of the fixed pipeline 48 is connected with the water inlet pipeline of the oil discharge pump 6, the flow guiding effect of the fixed pipeline 48 is improved, the oil-water separation membrane 49 is arranged on the inner groove wall of the negative pressure plate 44, the fixing effect of the oil-water separation membrane 49 is improved, the bottom of the inner groove of the negative pressure plate 44 is fixedly connected with the second oil absorption cotton 410, the fixing effect of the second oil absorption cotton 410 is improved, the negative pressure pump 41 and the regulating liquid rod 45 are electrically connected with the control panel 8, the flow guiding mechanism 5 is arranged inside the separation box 1, the telescopic length of the telescopic pipeline 43 is the same as the regulating range of the regulating liquid rod 45, the negative pressure plate 44 is in parallel relation with the inner top of the separation box 1, the regulating length of the regulating liquid rod 45 is improved, the first oil absorption cotton 47 and the second oil absorption cotton 410 are both oil filter layers with the thickness of 10 cm, and the second oil absorption cotton 410 is in parallel relation with the oil-water separation membrane 49, so that the oil absorption separation effect of the first oil absorption cotton 47 and the second oil absorption cotton 410 is improved.
Referring to fig. 4 and 5, the utility model provides a special crude benzene oil-water separator for coke chemical production workshop, the diversion mechanism 5 includes a heat conduction ring plate 51, a first electromagnetic directional valve 52, a temperature sensor 53, an electric heating liquid tank 54, a condensate liquid tank 55, a second electromagnetic directional valve 56, a heat conduction pump 57 and a return pipe 58, the inner wall of the separation box 1 is connected with the heat conduction ring plate 51 by bolts, the fixing effect of the heat conduction ring plate 51 is improved, the left top side opening of the heat conduction ring plate 51 is connected with the top connecting pipe of the first electromagnetic directional valve 52 by a pipeline, the diversion effect of the first electromagnetic directional valve 52 is improved, the top connecting pipe of the first electromagnetic directional valve 52 is connected with the temperature sensor 53 by bolts, the fixing effect of the temperature sensor 53 is improved, the opening at the front side of the first electromagnetic directional valve 52 is connected with the top pipe of the electric heating liquid tank 54, the fixing effect of the electric heating liquid tank 54 is improved, the electric heating liquid tank 54 is connected with the left side wall of the separation box 1 by bolts, the fixing effect of the electric heating liquid tank 54 is improved, the opening on the rear side of the first electromagnetic directional valve 52 is connected with the top pipeline of the condensate liquid tank 55, the flow guiding effect of the first electromagnetic directional valve 52 is improved, the condensate liquid tank 55 is connected with the left side wall of the separation box 1 through bolts, the fixing effect of the condensate liquid tank 55 is improved, the openings at the bottoms of the electric heating liquid tank 54 and the condensate liquid tank 55 are both connected with the water outlet pipeline of the second electromagnetic directional valve 56, the flow guiding effect of the second electromagnetic directional valve 56 is improved, the bottom of the second electromagnetic directional valve 56 is connected with the top opening pipeline of the heat conduction pump 57, the flow guiding effect of the heat conduction pump 57 is improved, the bottom water inlet of the heat conduction pump 57 is connected with the return pipe 58 through a pipeline, the flow guiding effect of the heat conduction pump 57 is improved, the return pipe 58 is connected with the right bottom opening pipeline of the heat conduction annular plate 51, the return effect of the return pipe 58 is improved, the first electromagnetic directional valve 52, the temperature sensor 53 and the electric heating liquid tank 54, The condensate tank 55, the second electromagnetic directional valve 56 and the heat conduction pump 57 are all electrically connected with the control panel 8, the diameter and the length of the water filtering ring 46 are the same as the diameter of an inner groove of the heat conduction ring plate 51, the heat conduction ring plate 51 is perpendicular to the inner wall of the water filtering ring 46, the water filtering effect of the water filtering ring 46 is improved, the first electromagnetic directional valve 52 and the second electromagnetic directional valve 56 are symmetrically distributed, the thickness of the heat conduction ring plate 51 is 5 cm, and the flow guiding effect of the first electromagnetic directional valve 52 and the second electromagnetic directional valve 56 is improved.
The utility model provides a special crude benzene oil-water separator for a coking chemical workshop through improvement, and the working principle is as follows;
firstly, when the equipment is used, the device is firstly placed in a working area, and then the equipment is connected with an external power supply, so that the required electric energy can be provided for the work of the equipment;
secondly, during the separation action, a worker adds an oil-water mixture containing crude benzene into the filter box 2 through the liquid inlet 3, and performs sundry filtration action on the oil-water mixture through the filter assembly 9 in the filter box, then the oil-water mixture enters the separation box 1 and gathers on the top of the negative pressure plate 44 and the water filtering ring 46, and then the control panel 8 controls the heat conduction pump 57, the first electromagnetic directional valve 52 and the second electromagnetic directional valve 56 to work, so that the heat conduction pump 57 drives the heat conduction oil in the return pipe 58 to enter the condensate box 55, and the condensation work is performed through the condensation part in the condensate box 55, so that the heat conduction oil in the condensate box 55 enters the heat conduction ring plate 51 through the first electromagnetic directional valve 52, and contacts with the oil-water mixture through the heat conduction ring plate 51 to perform heat conduction action;
thirdly, temperature monitoring is carried out through the temperature sensor 53, so that the internal temperature of the separation box 1 is controlled to be kept in a proper interval, the crystallization point of crude benzene oil is high, partial crystallization of oil substances in the oil-water mixture is caused, at the moment, moisture in the oil-water mixture enters the bottom space of the negative pressure plate 44 through the water filtering ring 46, the passing moisture is filtered again through the first oil absorption cotton 47, and the height of the negative pressure plate 44 is adjusted through the liquid adjusting rod 45, so that the water filtering ring 46 is prevented from being blocked by crystals;
fourthly, when the negative pressure plate 44 drives the water filtering ring 46 to contact with the heat conducting ring plate 51, the oil substances on the heat conducting ring plate 51 can be scraped by the water filtering ring 46, and then extracted by the components such as the negative pressure pump 41, the negative pressure pipeline 42 and the like, so that the opening at the bottom of the negative pressure plate 44 extracts water and sequentially passes through the oil-water separation membrane 49 and the second oil absorption cotton 410, further filtering action on the water is favorably improved, and the water is driven by pressure to enter the telescopic pipeline 43 and the negative pressure pipeline 42 and finally flows into the water storage tank 10 to be gathered;
fifthly, after moisture is extracted, the heat conduction oil in the electric liquid heating tank 54 is driven to enter the heat conduction annular plate 51 through the flow guiding effect of the heat conduction pump 57, the first electromagnetic directional valve 52 and the second electromagnetic directional valve 56, so that the overall temperature in the separation tank 1 is increased, the oil substance in the separation tank 1 is changed into a fluid state again, the oil substance is extracted through the oil drainage pump 6 and the fixed pipeline 48, and the negative pressure plate 44 and the fixed pipeline 48 at the top of the negative pressure plate can be driven to be adjusted in height through the adjusting liquid rod 45, and the oil substance is extracted.
The utility model relates to a special crude benzol water oil separator in coke chemical workshop, through optimizing and driving negative pressure pipeline 42 and flexible pipeline 43 and the inside air current outflow of negative pressure plate 44 through negative pressure pump 41, at this moment, carry out the primary separation action to the profit through filtering water ring 46 and first oil absorption cotton 47, and then utilize atmospheric pressure to improve and shunt rivers through oil-water separation membrane 49 and second oil absorption cotton 410, be favorable to improving the effect of taking out moisture, simultaneously carry out the displacement adjustment action to negative pressure plate 44 and water filtration ring 46 through adjusting liquid pole 45, be favorable to improving the many times filtering separation effect to the profit, through the water conservancy diversion action between heat conduction pump 57 and first electromagnetic directional valve 52 and second electromagnetic directional valve 56 make the heat conduction oil inside condensate tank 55 get into the inside heat conduction ring board 51, thereby carry out the condensation action to the profit inside separation tank 1, thereby make the higher crude benzol oil of crystallization point take place the crystallization and filtered the action by parts such as drainage ring 46, after the water is extracted, the heat conducting oil in the electric heating liquid tank 54 enters the heat conducting annular plate 51 through the flow guide of the electric heating liquid tank, so that the crude benzene oil reaching the crystallization point returns to a liquid state again, and the temperature control effect of oil-water separation and the auxiliary effect of separation are favorably improved.
Claims (8)
1. The utility model provides a dedicated crude benzol oil water separator in coke chemical industry workshop, includes separator box (1) and storage water tank (10), separator box (1) top and rose box (2) bottom pipe connection, rose box (2) left side is equipped with inlet (3), separator box (1) top and oil extraction pump (6) bolted connection, separator box (1) front end and sealed maintenance door (7) hinged joint, its characterized in that: the device is characterized by further comprising an adjusting mechanism (4) and a flow guide mechanism (5), wherein the adjusting mechanism (4) is arranged on the right side of the separation box (1), the adjusting mechanism (4) comprises a negative pressure pump (41), a negative pressure pipeline (42), a telescopic pipeline (43), a negative pressure plate (44), a regulating liquid rod (45), a water filtering ring (46), first oil absorption cotton (47), a fixed pipeline (48), an oil-water separation membrane (49) and second oil absorption cotton (410), an opening in the top of the negative pressure pump (41) is connected with the negative pressure pipeline (42) through a pipeline, the negative pressure pipeline (42) is connected with the top pipeline of the telescopic pipeline (43), the left side and the right side of the bottom of the negative pressure plate (44) are connected with the regulating liquid rod (45) through bolts, the first oil absorption cotton (47) is arranged at the bottom of the water filtering ring (46), the right side of the top of the water filtering ring (46) is connected with the bottom of the fixed pipeline (48) through bolts, a separation membrane (49) is arranged in an inner groove of the oil-water plate (44), the bottom of an inner groove of the negative pressure plate (44) is fixedly connected with a second oil absorption cotton (410), and the flow guide mechanism (5) is arranged inside the separation box (1).
2. The special crude benzene oil-water separator for the coking production workshop according to claim 1, characterized in that: the flow guide mechanism (5) comprises a heat conduction ring plate (51), a first electromagnetic directional valve (52), a temperature sensor (53), an electric heating liquid tank (54), a condensate liquid tank (55), a second electromagnetic directional valve (56), a heat conduction pump (57) and a return pipe (58), wherein the inner wall of the separation tank (1) is in bolted connection with the heat conduction ring plate (51), the opening on the left top side of the heat conduction ring plate (51) is connected with a connecting pipe at the top of the first electromagnetic directional valve (52), the connecting pipe at the top of the first electromagnetic directional valve (52) is in bolted connection with the temperature sensor (53), the opening on the front side of the first electromagnetic directional valve (52) is connected with a top pipe of the electric heating liquid tank (54), the electric heating liquid tank (54) is in bolted connection with the left side wall of the separation tank (1), the opening on the rear side of the first electromagnetic directional valve (52) is connected with a top pipe of the condensate liquid tank (55), the condensate tank (55) is in bolted connection with the left side wall of the separation tank (1), openings at the bottoms of the electric heating liquid tank (54) and the condensate tank (55) are connected with a water outlet pipeline of a second electromagnetic directional valve (56), the bottom of the second electromagnetic directional valve (56) is connected with a top opening pipeline of a heat conduction pump (57), a water inlet at the bottom of the heat conduction pump (57) is connected with a return pipe (58) through a pipeline, the return pipe (58) is connected with a right bottom opening pipeline of a heat conduction ring plate (51), and the first electromagnetic directional valve (52), the temperature sensor (53), the electric heating liquid tank (54), the condensate tank (55), the second electromagnetic directional valve (56) and the heat conduction pump (57) are electrically connected with the control panel (8).
3. The special crude benzene oil-water separator for the coking production workshop according to claim 1, characterized in that: sealed maintenance door (7) front end and control panel (8) bolted connection, rose box (2) inner wall and filtering component (9) bolted connection, separator box (1) right side bottom and storage water tank (10) bolted connection, oil extraction pump (6) are connected with control panel (8) electricity.
4. The special crude benzene oil-water separator for the coking production workshop as claimed in claim 1, wherein: separator box (1) right side and negative pressure pump (41) bolted connection, negative pressure pump (41) bottom opening and storage water tank (10) top pipe connection, negative pressure pipeline (42) and rose box (2) top opening pipe connection, negative pressure pipeline (42) and filtering component (9) centre of a circle through-hole fixed connection, flexible pipeline (43) bottom and negative pressure board (44) top middle part opening pipe connection, regulation liquid pole (45) and separator box (1) bottom opening fixed connection, negative pressure board (44) outside and filter ring (46) inner ring wall bolted connection, fixed pipeline (48) top and oil extraction pump (6) water inlet pipe connection, negative pressure pump (41) and regulation liquid pole (45) all are connected with control panel (8) electricity.
5. The special crude benzene oil-water separator for the coking production workshop according to claim 1, characterized in that: the telescopic length of the telescopic pipeline (43) is the same as the adjusting stroke of the adjusting liquid rod (45), and the negative pressure plate (44) is parallel to the inner top of the separation box (1).
6. The special crude benzene oil-water separator for the coking production workshop as claimed in claim 1, wherein: the first oil absorption cotton (47) and the second oil absorption cotton (410) are both oil filter layers with the thickness of 10 cm, and the second oil absorption cotton (410) and the oil-water separation membrane (49) are in parallel relation.
7. The special crude benzene oil-water separator for the coking production workshop according to claim 1, characterized in that: the diameter and the length of the water filtering ring (46) are the same as the diameter of an inner groove of the heat conducting ring plate (51), and the heat conducting ring plate (51) is perpendicular to the inner wall of the water filtering ring (46).
8. The special crude benzene oil-water separator for the coking production workshop according to claim 2, characterized in that: the first electromagnetic directional valve (52) and the second electromagnetic directional valve (56) are symmetrically distributed, and the thickness of the heat conducting annular plate (51) is 5 cm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220278493.5U CN216825196U (en) | 2022-02-10 | 2022-02-10 | Dedicated crude benzene oil water separator in coke chemical industry workshop |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220278493.5U CN216825196U (en) | 2022-02-10 | 2022-02-10 | Dedicated crude benzene oil water separator in coke chemical industry workshop |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216825196U true CN216825196U (en) | 2022-06-28 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202220278493.5U Active CN216825196U (en) | 2022-02-10 | 2022-02-10 | Dedicated crude benzene oil water separator in coke chemical industry workshop |
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| Country | Link |
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| CN (1) | CN216825196U (en) |
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2022
- 2022-02-10 CN CN202220278493.5U patent/CN216825196U/en active Active
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