CN207741607U - A kind of waste oil regeneration rectifying catalysis system residual heat using device - Google Patents
A kind of waste oil regeneration rectifying catalysis system residual heat using device Download PDFInfo
- Publication number
- CN207741607U CN207741607U CN201721751288.1U CN201721751288U CN207741607U CN 207741607 U CN207741607 U CN 207741607U CN 201721751288 U CN201721751288 U CN 201721751288U CN 207741607 U CN207741607 U CN 207741607U
- Authority
- CN
- China
- Prior art keywords
- cooling tank
- waste oil
- oil
- tank
- waste
- 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.)
- Withdrawn - After Issue
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
A kind of waste oil regeneration rectifying catalysis system residual heat using device of the utility model is related to used oil reclaimer.A kind of waste oil regeneration rectifying catalysis system residual heat using device, surge tank is overlapped on water cooling tank, oily cooling tank is overlapped on surge tank, oily cooling tank coil pipe is equipped in oily cooling tank, it is equipped with waste oil import on the side wall of oily cooling tank and waste oil exports, it is equipped with water cooling tank coil pipe in water cooling tank, has a surplus recovery tubes in oil gas efferent duct housing, the waste oil outlet after heating is equipped in waste heat recovery pipe.The waste oil regeneration rectifying catalysis system residual heat using device of the utility model, reasonable for structure, securely and reliably, it can make full use of the waste heat of oil gas in waste oil regeneration rectifying catalysis system to preheat waste oil；Waste oil can be heated to spend 100 DEG C from room temperature more, significantly reduce the energy consumption of rectifying catalytic regeneration waste oil, and significant decrease production cost is higher, energy saving, has promotional value.
Description
Technical field
The utility model is related to arrive used oil reclaimer, it is more particularly to a kind of waste oil regeneration rectifying catalysis system waste heat
Utilize device.
Background technology
In waste oil regeneration, needs for waste oil to be heated to certain temperature, heat the temperature of waste oil, need according to waste oil again
Depending on raw kind and regeneration technology.In rectifying catalytic regeneration waste oil, needs waste oil being heated to 200 DEG C -400 DEG C, make to give up
Then the oil of gasification is quickly cooled down the oil for becoming liquid by fry dried food ingredients anger.In the past, it is to use to follow that the oil of gasification, which was quickly cooled down,
Ring water is cooled down, and recirculated water needs to be cooled down in great Chi again, and the waste heat of the oil of gasification fails to make full use of, and causes rectifying
The energy consumption of catalytic regeneration waste oil is higher, and production cost is higher, in order to energy saving, the cost of reduction rectifying catalytic regeneration waste oil,
Need to be explored a kind of waste oil regeneration rectifying catalysis system residual heat using device.
Invention content
The purpose of this utility model provides a kind of waste oil regeneration rectifying catalysis system residual heat using device.
The technical solution of the utility model：A kind of waste oil regeneration rectifying catalysis system residual heat using device, which is characterized in that
Surge tank is overlapped on water cooling tank, oily cooling tank is overlapped on surge tank, oily cooling tank disk is equipped in oily cooling tank
Pipe, is equipped with waste oil import on the side wall of oily cooling tank and waste oil exports, and water cooling tank coil pipe is equipped in water cooling tank, in water
The side wall of cooling tank is equipped with cooling water inlet and cooling water outlet, and waste heat recovery pipe is cased in transportation pipe, outer wall,
The outlet of transportation pipe is connected to by oil and gas import with the upper end of oily cooling tank coil pipe, the outlet and buffering of oily cooling tank coil pipe
The outlet of the inlet communication of tank, surge tank is connected to the upper end of water cooling tank coil pipe, the lower end of water cooling tank coil pipe and oil export
It is connected to, the waste oil outlet on oily cooling tank is connected to one end of waste heat recovery pipe, and heating is equipped in the other end of waste heat recovery pipe
Waste oil outlet afterwards.
The waste oil regeneration rectifying catalysis system residual heat using device, described in oily cooling tank, surge tank and water cooling
But tank is vertically connected, and oil level glass is equipped on the side wall of surge tank.
Waste oil regeneration rectifying catalysis system residual heat using device described above, described in waste heat recovery pipe it is horizontally disposed
In the top of oily cooling tank, waste oil outlet is located at the top of oily cooling tank, and waste oil import is located at the lower part of oily cooling tank, cooling water
Import is located at the top of water cooling tank, and cooling water outlet is located at the lower part of water cooling tank.
The operation principle of the utility model：It needs the waste oil heated to enter oily cooling tank from waste oil import, absorbs oil cooling but
Heat on tank coil pipe, and the one end for exiting into waste heat recovery pipe is exported from waste oil, the heat on transportation pipe is reabsorbed,
Then discharge is exported from the waste oil after the heating of the other end of waste heat recovery pipe.Generally, the oil gas temperature in transportation pipe is high
It is spent up to 300 DEG C more, after oil gas absorbs heat by the waste oil in waste heat recovery pipe, drops at a temperature of oil gas and spent 200 DEG C more, oil gas
Oily cooling tank coil pipe is entered back into, after oil gas absorbs heat by waste oil again in oily cooling tank, temperature drops to be spent more 100 DEG C, then
Into surge tank, oil gas essentially becomes the oil of liquid, after oil enters back into water cooling tank coil pipe, and is cooled directly with water the absorption of the water in tank
After heat, temperature drops to be spent more 40 DEG C, and oil is finally discharged from oil export.
The beneficial effects of the utility model：A kind of waste oil regeneration rectifying catalysis system UTILIZATION OF VESIDUAL HEAT IN of the utility model fills
It sets, reasonable for structure, securely and reliably, it can make full use of the waste heat of oil gas in waste oil regeneration rectifying catalysis system to preheat waste oil；
Waste oil can be heated to spend 100 DEG C from room temperature more, significantly reduce the energy consumption of rectifying catalytic regeneration waste oil, significant decrease is produced into
This is higher, energy saving, has promotional value.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model；
It is marked in figure：Cooling water inlet 1, water cooling tank 2, water cooling tank coil pipe 3, cooling water outlet 4, surge tank 5, waste oil
Import 6, oily cooling tank coil pipe 7, oily cooling tank 8, waste oil outlet 9, oil and gas import 10, waste heat recovery pipe 11, transportation pipe 12,
Waste oil outlet 13 after heating, oil export 14.
Specific implementation mode
Below by embodiment, the utility model is further described.
Embodiment 1
Referring to Fig.1, a kind of waste oil regeneration rectifying catalysis system residual heat using device, overlaps with buffering on water cooling tank 2
Tank 5 overlaps with oily cooling tank 8 on surge tank 5, oily cooling tank coil pipe 7 is equipped in oily cooling tank 8, in the side of oily cooling tank 8
Wall is equipped with waste oil import 6 and waste oil outlet 9, water cooling tank coil pipe 3 is equipped in water cooling tank 2, in the side wall of water cooling tank 2
It is equipped with cooling water inlet 1 and cooling water outlet 4, is cased with waste heat recovery pipe 11 in 12 ability of transportation pipe, outer wall, oil gas is defeated
The outlet of pipe 12 is sent to be connected to the upper end of oily cooling tank coil pipe 7 by oil and gas import 10, the outlet and buffering of oily cooling tank coil pipe 7
The outlet of the inlet communication of tank 5, surge tank 5 is connected to the upper end of water cooling tank coil pipe 3, lower end and the oil of water cooling tank coil pipe 3
Outlet 14 is connected to, and the waste oil outlet 9 on oily cooling tank 8 is connected to one end of waste heat recovery pipe 11, in the another of waste heat recovery pipe 11
One end is equipped with the waste oil outlet 13 after heating.
Embodiment 2
Referring to Fig.1, a kind of waste oil regeneration rectifying catalysis system residual heat using device, overlaps with buffering on water cooling tank 2
Tank 5 overlaps with oily cooling tank 8 on surge tank 5, oily cooling tank coil pipe 7 is equipped in oily cooling tank 8, in the side of oily cooling tank 8
Wall is equipped with waste oil import 6 and waste oil outlet 9, water cooling tank coil pipe 3 is equipped in water cooling tank 2, in the side wall of water cooling tank 2
It is equipped with cooling water inlet 1 and cooling water outlet 4, is cased with waste heat recovery pipe 11 in 12 ability of transportation pipe, outer wall, oil gas is defeated
The outlet of pipe 12 is sent to be connected to the upper end of oily cooling tank coil pipe 7 by oil and gas import 10, the outlet and buffering of oily cooling tank coil pipe 7
The outlet of the inlet communication of tank 5, surge tank 5 is connected to the upper end of water cooling tank coil pipe 3, lower end and the oil of water cooling tank coil pipe 3
Outlet 14 is connected to, and the waste oil outlet 9 on oily cooling tank 8 is connected to one end of waste heat recovery pipe 11, in the another of waste heat recovery pipe 11
One end is equipped with the waste oil outlet 13 after heating.Oily cooling tank 8, surge tank 5 and the water cooling tank 2 is vertically connected,
The side wall of surge tank 5 is equipped with oil level glass.
Embodiment 3
Referring to Fig.1, a kind of waste oil regeneration rectifying catalysis system residual heat using device, overlaps with buffering on water cooling tank 2
Tank 5 overlaps with oily cooling tank 8 on surge tank 5, oily cooling tank coil pipe 7 is equipped in oily cooling tank 8, in the side of oily cooling tank 8
Wall is equipped with waste oil import 6 and waste oil outlet 9, water cooling tank coil pipe 3 is equipped in water cooling tank 2, in the side wall of water cooling tank 2
It is equipped with cooling water inlet 1 and cooling water outlet 4, is cased with waste heat recovery pipe 11 in 12 ability of transportation pipe, outer wall, oil gas is defeated
The outlet of pipe 12 is sent to be connected to the upper end of oily cooling tank coil pipe 7 by oil and gas import 10, the outlet and buffering of oily cooling tank coil pipe 7
The outlet of the inlet communication of tank 5, surge tank 5 is connected to the upper end of water cooling tank coil pipe 3, lower end and the oil of water cooling tank coil pipe 3
Outlet 14 is connected to, and the waste oil outlet 9 on oily cooling tank 8 is connected to one end of waste heat recovery pipe 11, in the another of waste heat recovery pipe 11
One end is equipped with the waste oil outlet 13 after heating.Oily cooling tank 8, surge tank 5 and the water cooling tank 2 is vertically connected,
The side wall of surge tank 5 is equipped with oil level glass.The waste heat recovery pipe 11 is horizontally set on the top of oily cooling tank 8, gives up
Oil export 9 is located at the top of oily cooling tank 8, and waste oil import 6 is located at the lower part of oily cooling tank 8, and cooling water inlet 1 is located at water cooling
The top of tank 2, cooling water outlet 4 are located at the lower part of water cooling tank 2.
Claims (3)
1. a kind of waste oil regeneration rectifying catalysis system residual heat using device, which is characterized in that in water cooling tank（2）On overlap with it is slow
Rush tank（5）, in surge tank（5）On overlap with oily cooling tank（8）, in oily cooling tank（8）It is interior to be equipped with oily cooling tank coil pipe（7）,
Oily cooling tank（8）Side wall be equipped with waste oil import（6）It is exported with waste oil（9）, in water cooling tank（2）It is interior to be equipped with water cooling tank disk
Pipe（3）, in water cooling tank（2）Side wall be equipped with cooling water inlet（1）And cooling water outlet（4）, in transportation pipe（12）
, outer wall is cased with waste heat recovery pipe（11）, transportation pipe（12）Outlet pass through oil and gas import（10）With oily cooling tank disk
Pipe（7）Upper end connection, oily cooling tank coil pipe（7）Outlet and surge tank（5）Inlet communication, surge tank（5）Outlet with
Water cooling tank coil pipe（3）Upper end connection, water cooling tank coil pipe（3）Lower end and oil export（14）Connection, oily cooling tank（8）On
Waste oil outlet（9）With waste heat recovery pipe（11）One end connection, in waste heat recovery pipe（11）The other end be equipped with heating after
Waste oil exports（13）.
2. waste oil regeneration rectifying catalysis system residual heat using device according to claim 1, which is characterized in that the oil
Cooling tank（8）, surge tank（5）With water cooling tank（2）It is vertically connected, in surge tank（5）Side wall equipped with oil level observe
Window.
3. waste oil regeneration rectifying catalysis system residual heat using device according to claim 1 or 2, which is characterized in that described
Waste heat recovery pipe（11）It is horizontally set on oily cooling tank（8）Top, waste oil outlet（9）Positioned at oily cooling tank（8）Top,
Waste oil import（6）Positioned at oily cooling tank（8）Lower part, cooling water inlet（1）Positioned at water cooling tank（2）Top, cooling water goes out
Mouthful（4）Positioned at water cooling tank（2）Lower part.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721751288.1U CN207741607U (en) | 2017-12-15 | 2017-12-15 | A kind of waste oil regeneration rectifying catalysis system residual heat using device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721751288.1U CN207741607U (en) | 2017-12-15 | 2017-12-15 | A kind of waste oil regeneration rectifying catalysis system residual heat using device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207741607U true CN207741607U (en) | 2018-08-17 |
Family
ID=63118094
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721751288.1U Withdrawn - After Issue CN207741607U (en) | 2017-12-15 | 2017-12-15 | A kind of waste oil regeneration rectifying catalysis system residual heat using device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207741607U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107860249A (en) * | 2017-12-15 | 2018-03-30 | 重庆方盛净化设备有限公司 | Waste oil regeneration rectifying catalysis system residual heat using device |
| CN109621876A (en) * | 2019-01-24 | 2019-04-16 | 江西立德传动设备有限公司 | A kind of liquid material combination cooling device |
-
2017
- 2017-12-15 CN CN201721751288.1U patent/CN207741607U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107860249A (en) * | 2017-12-15 | 2018-03-30 | 重庆方盛净化设备有限公司 | Waste oil regeneration rectifying catalysis system residual heat using device |
| CN107860249B (en) * | 2017-12-15 | 2023-09-19 | 重庆方盛净化设备有限公司 | Waste heat utilization device of waste oil regeneration rectification catalytic system |
| CN109621876A (en) * | 2019-01-24 | 2019-04-16 | 江西立德传动设备有限公司 | A kind of liquid material combination cooling device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN207741607U (en) | A kind of waste oil regeneration rectifying catalysis system residual heat using device | |
| CN103604233A (en) | Process and system for using waste heat of steam of steam box | |
| CN204301574U (en) | A kind of novel hot water feeding mechanism | |
| CN203927881U (en) | A kind of oil-burning gas-fired boiler energy-saving appliance | |
| CN201755493U (en) | Circulation cooling system for reaction kettle | |
| CN205245139U (en) | Highly -effective steam generator | |
| CN101992914A (en) | Train oil tank rapid discharging heating device and heating method thereof | |
| CN104018010B (en) | Reduction and distillation furnace in titanium sponge production | |
| CN103884098B (en) | Waste heat recovery air source water heater | |
| CN202440743U (en) | Asphalt heating device of mixing unit | |
| CN203908371U (en) | Flue gas waste heat recovery device | |
| CN203614179U (en) | Gas electrical generation waste heat recovery device | |
| CN107860249A (en) | Waste oil regeneration rectifying catalysis system residual heat using device | |
| CN202762414U (en) | Glycol regenerating device | |
| CN203700458U (en) | Reduction distilling furnace for producing titanium sponge by virtue of magnesium reduction method | |
| CN203034018U (en) | Cooling water recycling system of fermentation tank | |
| CN203375859U (en) | Waste water waste heat recovery tank | |
| CN208703953U (en) | A kind of boiler afterheat reclaimer | |
| CN203629109U (en) | Steam box steam waste heat utilization system | |
| CN203798205U (en) | Industrial waste gas waste heat-recycling heat exchanging device | |
| CN207540393U (en) | It is a kind of to prepare coal-fired flue-gas waste heat recovery circulator in lithium carbonate technique | |
| CN203529927U (en) | Anhydrous hydrogen fluoride production equipment | |
| CN207701210U (en) | A kind of jet dynamic control tail gas waste heat utilizing device | |
| CN203028993U (en) | Heating system for water dispenser | |
| CN205418884U (en) | Slop conveyor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20180817 Effective date of abandoning: 20230919 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20180817 Effective date of abandoning: 20230919 |