CN209940912U - Petroleum is refined with petroleum distillation plant - Google Patents
Petroleum is refined with petroleum distillation plant Download PDFInfo
- Publication number
- CN209940912U CN209940912U CN201920588587.0U CN201920588587U CN209940912U CN 209940912 U CN209940912 U CN 209940912U CN 201920588587 U CN201920588587 U CN 201920588587U CN 209940912 U CN209940912 U CN 209940912U
- Authority
- CN
- China
- Prior art keywords
- pipe
- heating chamber
- petroleum
- chamber
- heating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000003208 petroleum Substances 0.000 title claims abstract description 15
- 238000004525 petroleum distillation Methods 0.000 title claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 55
- 238000010438 heat treatment Methods 0.000 claims abstract description 53
- 238000001816 cooling Methods 0.000 claims abstract description 36
- 238000007670 refining Methods 0.000 claims abstract 4
- 230000001681 protective effect Effects 0.000 claims description 10
- 238000005504 petroleum refining Methods 0.000 claims description 4
- 238000007599 discharging Methods 0.000 abstract description 11
- 238000009833 condensation Methods 0.000 abstract description 10
- 230000005494 condensation Effects 0.000 abstract description 10
- 238000004821 distillation Methods 0.000 abstract description 7
- 239000007789 gas Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 4
- 239000002912 waste gas Substances 0.000 description 4
- 238000003912 environmental pollution Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000000605 extraction Methods 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 150000003464 sulfur compounds Chemical class 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a petroleum distillation plant for refining petroleum, which comprises a heating chamber, a controller is arranged at one side of the heating chamber, an oil inlet is arranged at one side of the heating chamber close to the upper part of the controller, a heating groove is arranged at the bottom end of the heating chamber, a heating wire is arranged in the heating groove, an air chamber is fixed at the top part of the heating chamber, an air inlet pipe penetrates between the heating chamber and the air chamber, a fan is fixedly connected with the inside of the air chamber through a bracket, the utility model discloses a circulating water pump draws out cold water in a water tank and conveys the cold water into a cooling pipe, the cold water returns to the water tank after passing through the cooling pipe, the circulation is repeated, condensed oil body flows into a through pipe along the inner wall of a discharging pipe, and then enters an oil collecting tank through the through pipe, thereby realizing the cooling and condensation of steam, and simultaneously avoiding, the working efficiency during distillation is improved.
Description
Technical Field
The utility model belongs to the technical field of the oil distillation, concretely relates to petroleum is refined and is used petroleum distillation plant.
Background
The petroleum distillation is a mixture of over 8000 kinds of hydrocarbons (and a small amount of sulfur compounds) with different molecular sizes, and before use, the petroleum must be processed to make petroleum products suitable for various purposes.
In chinese patent No. CN201721151424.3, a petroleum distillation apparatus for petroleum refining is disclosed, which describes that "starting an air pump pumps air in a thermal insulation box through a refrigeration block into an air inlet pipe and pumps the air out through an air outlet pipe, the cold air rushes out a second cover plate and enters the air chamber through a second air guide hole, and the petroleum steam in the air chamber is cooled to a certain extent, thereby achieving a cooling effect", but in the using process of the method, because the time of the petroleum distillation process is long, the cold air refrigerated in the thermal insulation box is limited, and cannot provide cooling for a long time, and the cold air may directly act with steam in the air chamber, so that the condensed oil directly returns to a heating chamber, and in addition, a waste gas collecting device is not provided, the petroleum can generate a large amount of waste gas in the distillation process, and is not collected and directly discharged to the outside, thereby causing environmental pollution, endangering the life and health of people.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a petroleum refines and uses petroleum distillation plant to solve the unable long term effectual cooling that proposes in the above-mentioned background art, the oil body of condensation can directly get back to in the heating chamber, and does not set up the problem of collecting exhaust gas device.
In order to achieve the above object, the utility model provides a following technical scheme: a petroleum distillation device for petroleum extraction comprises a heating chamber, wherein a controller is installed on one side of the heating chamber, an oil inlet is formed in one side of the heating chamber close to the upper portion of the controller, a heating groove is formed in the bottom end of the inside of the heating chamber, heating wires are installed inside the heating groove, an air chamber is fixed to the top of the heating chamber, an air inlet pipe penetrates through the heating chamber and the air chamber, a fan is fixedly connected to the inside of the air chamber through a support, a discharging pipe is installed on one side of the air chamber, a cooling pipe is sleeved on the outer wall of one end, away from the air chamber, of the discharging pipe, a protective cover is fixed to the outside of the cooling pipe, an oil collecting tank is installed below the protective cover, a through pipe is connected between the oil collecting tank and the protective cover, one end, extending to, the water tank is installed to one side of heating chamber, the water tank passes through the pipeline and communicates with the circulating water pump, the water inlet of cooling tube with pass through the pipeline and be connected with the circulating water pump, and the delivery port of cooling tube is connected with the water tank through the pipeline.
Preferably, an exhaust pipe is installed on one side of the discharge pipe, an exhaust pump is connected to one end, far away from the discharge pipe, of the exhaust pipe, and a gas collection tank is connected to one side of the exhaust pump through a hose.
Preferably, the cooling pipe is of an S-shaped structure, and the vertical section of the cooling pipe is of a circular structure.
Preferably, a filter screen is installed at one end, close to the air exhaust pipe, of the interior of the discharge pipe, and a double-layer filter screen layer is arranged inside the filter screen.
Preferably, a rubber pad is installed at the bottom of the heating chamber, and an anti-slip groove is formed in the outer wall of the rubber pad.
Compared with the prior art, the beneficial effects of the utility model are that:
(1) the utility model discloses a during circulating water pump takes the cold water in with the water tank out and carries into the cooling tube, in cold water got back to the water tank again behind the cooling tube, so the circulation repeatedly, during the oil body after the condensation flowed into the siphunculus along the inner wall of discharging pipe, and in the back got into the sump oil tank through the siphunculus, and then realized the cooling condensation of steam, during the oil body after having avoided the condensation simultaneously got back to the heating chamber, work efficiency when having improved the distillation.
(2) The utility model discloses a waste gas in the discharge tube is taken out to the aspiration pump, and the gas that is taken out is carried into the gas collecting box through the aspiration pump in, and then has realized gaseous collection, has avoided the environmental pollution that direct emission caused, has improved factor of safety.
Drawings
Fig. 1 is a schematic structural view of the present invention;
FIG. 2 is a schematic view of the internal structure of the present invention;
FIG. 3 is an enlarged view of portion A of FIG. 2;
fig. 4 is a circuit block diagram of the present invention;
in the figure: 1-a heating chamber; 2-a controller; 3, rubber cushion; 4-an oil inlet; 5-air chamber; 6-a fan; 7-an air inlet pipe; 8-a discharge pipe; 9-a water tank; 10-a protective cover; 11-a cooling tube; 12-a through pipe; 13-an oil collecting tank; 14-a circulating water pump; 15-filtering with a filter screen; 16-an extraction tube; 17-an air pump; 18-a gas collection tank; 19-a heating tank; 20-heating wires.
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. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-4, the present invention provides the following technical solutions: a petroleum distillation device for petroleum refining comprises a heating chamber 1, a controller 2 is installed on one side of the heating chamber 1, the model of the controller 2 is a CPU226, the rated power is 11w, the working voltage is 24V, an oil inlet 4 is arranged on one side of the heating chamber 1 close to the upper side of the controller 2, the oil inlet 4 and the heating chamber 1 are of an integral structure, a heating groove 19 is formed in the bottom end inside the heating chamber 1, a heating wire 20 is installed inside the heating groove 19, the heating wire 20 is electrically connected with the controller 2, an air chamber 5 is fixed at the top of the heating chamber 1, an air inlet pipe 7 penetrates between the heating chamber 1 and the air chamber 5, a fan 6 is fixedly connected inside the air chamber 5 through a support, the fan 6 is electrically connected with the controller 2, the fan 6 is started through the controller 2, further the fan 6 sends steam generated by evaporation into a discharge pipe 8, the discharge pipe, one end outer wall cover that air chamber 5 was kept away from to discharging pipe 8 is equipped with cooling tube 11, cooling tube 11's external fixation has safety cover 10, safety cover 10 has the effect of protection cooling tube 11, play the effect of supporting circulating water pump 14 simultaneously, sump oil tank 13 is installed to the below of safety cover 10, be connected with siphunculus 12 between sump oil tank 13 and the safety cover 10, siphunculus 12 extends to the inside one end of safety cover 10 and goes outThe material pipe 8 is communicated, condensed oil body flows into the through pipe 12 along the inner wall of the material pipe 8 and then enters the oil collecting tank 13 through the through pipe 12, the top of the protective cover 10 is fixedly connected with a circulating water pump 14 through a bracket, the circulating water pump 14 is electrically connected with the controller 2, the circulating water pump 14 adopts a 50CQ-25 water pump, the voltage of the circulating water pump is 220 plus 380V, the rotating speed is 2900r/min, and the flow rate is 14.4m3H, a water tank 9 is installed on one side of the heating chamber 1, the water tank 9 is communicated with a circulating water pump 14 through a pipeline, a water inlet of a cooling pipe 11 is connected with the circulating water pump 14 through a pipeline, a water outlet of the cooling pipe 11 is connected with the water tank 9 through a pipeline, the circulating water pump 14 is started through the controller 2 to enable the circulating water pump 14 to work, the circulating water pump 14 pumps out cold water in the water tank 9 through a pipeline and conveys the cold water into the cooling pipe 11, the cold water returns to the water tank 9 after passing through the cooling pipe 11, the circulation is repeated, the cooling and condensation of steam are further realized, meanwhile, the oil body after condensation is prevented from returning to the heating chamber 1, and the working efficiency during distillation is improved.
Further, exhaust tube 16 is installed to one side of discharging pipe 8, and exhaust tube 16 keeps away from the one end of discharging pipe 8 and is connected with aspiration pump 17, and aspiration pump 17 and 2 electric connection of controller, the model of aspiration pump 17 is HG-120, power: 0.12kw, voltage: 220V, maximum wind pressure: 5.5kPa, minimum suction pressure: 5.0kPa, air volume: m is3The utility model discloses a gas collection box 16, including exhaust pump 17, controller 2, exhaust pipe 8, exhaust pump 17, exhaust pipe 18, exhaust pump 17, gas collection box 18, gas collection box.
Further, cooling tube 11 is S type structure, and cooling tube 11 twines at the outer wall of discharging pipe 8, increase heat radiating area that can be better for rate of heat dissipation, and cooling tube 11 perpendicular cross-section is circular structure.
Specifically, a filter screen 15 is installed at one end, close to the exhaust pipe 16, of the interior of the discharge pipe 8, the filter screen 15 has an effect of preventing oil drops from entering the exhaust pipe 16, a double-layer filter screen layer is arranged inside the filter screen 15, and the double-layer filter screen layer and the filter screen 15 are of an integrated structure.
Specifically, the bottom of the heating chamber 1 is provided with a rubber pad 3, and the outer wall of the rubber pad 3 is provided with an anti-slip groove.
The utility model discloses a theory of operation and use flow: the utility model discloses when using, at first switch on makes the device circular telegram, pour oil into heating chamber 1 from oil inlet 4, then start heater strip 20 through controller 2, make the device begin to carry out the work of distilling, steam that the distillation produced gets into in air chamber 5 from intake pipe 7, start fan 6 through controller 2, and then make fan 6 send the steam that evaporates into discharging pipe 8, then start circulating water pump 14 through controller 2, make circulating water pump 14 work, circulating water pump 14 takes out the cold water in water tank 9 through the pipeline and transports into cooling tube 11, cold water gets back to in water tank 9 again after cooling tube 11, so the repeated circulation, and then realize the cooling condensation of steam, avoided the oil body after the condensation to get back to in heating chamber 1 simultaneously, the work efficiency when having improved the distillation, the oil body after the condensation flows into siphunculus 12 along the inner wall of discharging pipe 8, then in through siphunculus 12 entering oil sump tank 13, start aspiration pump 17 through controller 2, during waste gas in the discharging pipe 8 was inhaled exhaust tube 16, then in air collecting box 18 was carried into through aspiration pump 17, and then realized gaseous collection, avoided the environmental pollution that direct emission caused, improved factor of safety.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (5)
1. The utility model provides a petroleum refining uses petroleum distillation plant, includes heating chamber (1), controller (2) are installed to one side of heating chamber (1), and the top that one side of heating chamber (1) is close to controller (2) is provided with oil inlet (4), heating bath (19) have been seted up to the inside bottom of heating chamber (1), the internally mounted of heating bath (19) has heater strip (20), the top of heating chamber (1) is fixed with air chamber (5), and runs through between heating chamber (1) and air chamber (5) has intake pipe (7), support fixedly connected with fan (6), its characterized in that are passed through to the inside of air chamber (5): a discharge pipe (8) is arranged on one side of the air chamber (5), a cooling pipe (11) is sleeved on the outer wall of one end, far away from the air chamber (5), of the discharge pipe (8), a protective cover (10) is fixed outside the cooling pipe (11), an oil collecting tank (13) is arranged below the protective cover (10), a through pipe (12) is connected between the oil collecting tank (13) and the protective cover (10), one end of the through pipe (12) extending to the inside of the protective cover (10) is communicated with the discharge pipe (8), the top of the protective cover (10) is fixedly connected with a circulating water pump (14) through a bracket, a water tank (9) is arranged on one side of the heating chamber (1), the water tank (9) is communicated with a circulating water pump (14) through a pipeline, the water inlet of the cooling pipe (11) is connected with a circulating water pump (14) through a pipeline, and the water outlet of the cooling pipe (11) is connected with the water tank (9) through a pipeline.
2. The apparatus for distilling petroleum for refining petroleum according to claim 1, wherein: an air suction pipe (16) is installed on one side of the discharge pipe (8), one end, far away from the discharge pipe (8), of the air suction pipe (16) is connected with an air suction pump (17), and one side of the air suction pump (17) is connected with a gas collection box (18) through a hose.
3. The apparatus for distilling petroleum for refining petroleum according to claim 1, wherein: the cooling pipe (11) is of an S-shaped structure, and the vertical section of the cooling pipe (11) is of a circular structure.
4. The petroleum refining petroleum distillation plant as defined in claim 2, wherein: a filter screen (15) is installed at one end, close to the air suction pipe (16), of the interior of the discharge pipe (8), and a double-layer filter screen layer is arranged inside the filter screen (15).
5. The apparatus for distilling petroleum for refining petroleum according to claim 1, wherein: the heating chamber is characterized in that a rubber pad (3) is installed at the bottom of the heating chamber (1), and an anti-slip groove is formed in the outer wall of the rubber pad (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920588587.0U CN209940912U (en) | 2019-04-27 | 2019-04-27 | Petroleum is refined with petroleum distillation plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920588587.0U CN209940912U (en) | 2019-04-27 | 2019-04-27 | Petroleum is refined with petroleum distillation plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209940912U true CN209940912U (en) | 2020-01-14 |
Family
ID=69130543
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920588587.0U Active CN209940912U (en) | 2019-04-27 | 2019-04-27 | Petroleum is refined with petroleum distillation plant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209940912U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113713469A (en) * | 2021-09-15 | 2021-11-30 | 张文学 | Petroleum is refined with petroleum distillation plant |
-
2019
- 2019-04-27 CN CN201920588587.0U patent/CN209940912U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113713469A (en) * | 2021-09-15 | 2021-11-30 | 张文学 | Petroleum is refined with petroleum distillation plant |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107960849B (en) | Steam box water recycling device | |
| CN206706059U (en) | A kind of cryogenic vacuum cycling extraction device of rose | |
| CN202675930U (en) | Steam condenser vacuumizing cooling device | |
| CN209940912U (en) | Petroleum is refined with petroleum distillation plant | |
| CN117699891A (en) | Recovery processing device for formaldehyde production cooling water | |
| CN211435156U (en) | Novel high-efficient vacuum cold trap | |
| CN104226013A (en) | Anhydrous condensation vacuum oil purifier | |
| CN207438671U (en) | A kind of range hood | |
| CN205939622U (en) | Air conditioner condensate recovering unit | |
| CN206478833U (en) | A kind of condensate water processing system of mobile air conditioner and the mobile air conditioner with it | |
| CN214142248U (en) | Device for efficiently extracting plant essential oil | |
| CN214039623U (en) | Yellow phosphorus slag water quenching steam collecting and discharging system | |
| CN214263259U (en) | Wire cooling device | |
| CN211060695U (en) | Steam recovery type energy-saving cooling tower | |
| CN209961060U (en) | Cooling plate structure for cooling tower | |
| CN208040671U (en) | A kind of integral type oilless (oil free) compressor | |
| CN206944741U (en) | A kind of even distribution type multi-stage, efficient condensing unit | |
| CN207307549U (en) | A kind of vacuum drying oven organic gas cools down retracting device | |
| CN213537276U (en) | Medical multifunctional oxygen generator | |
| CN105298680A (en) | Heat recovery device used for diesel generating set | |
| CN215216757U (en) | Spices condensing equipment | |
| CN207262974U (en) | Evaporation type vacuum condenser | |
| CN206175340U (en) | Energy -conserving high -efficient high -speed diffusion pump | |
| CN218276443U (en) | Frequency converter with heat radiation structure | |
| CN2608917Y (en) | Refrigerating working medium purifying device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20231116 Address after: 400000 Gaodong New Street, Yantai Town, Dianjiang County, Chongqing Patentee after: Chongqing Xiaoyun Environmental Protection Technology Co.,Ltd. Address before: 400000 Gaodong New Street, Yantai Town, Dianjiang County, Chongqing Patentee before: Chongqing Sheng Ke Energy Co.,Ltd. |