CN208104304U - A kind of mineral waste feedstock oil refinement system - Google Patents
A kind of mineral waste feedstock oil refinement system Download PDFInfo
- Publication number
- CN208104304U CN208104304U CN201820524651.4U CN201820524651U CN208104304U CN 208104304 U CN208104304 U CN 208104304U CN 201820524651 U CN201820524651 U CN 201820524651U CN 208104304 U CN208104304 U CN 208104304U
- Authority
- CN
- China
- Prior art keywords
- tank
- inlet
- communicated
- measuring
- receiving
- 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.)
- Expired - Fee Related
Links
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
A kind of mineral waste feedstock oil refinement system, it includes head tank (1), first reaction storage device, second reaction storage device and exhaust gas cleaner, first reaction storage device includes the first measuring tank (2), first auxiliary tank (3), first distillation still (4), A receiving tank (5), B receiving tank (6), first cooling tower (7), first taper storage tank (8) and surge tank (9), second reaction storage device includes the second measuring tank (10), second auxiliary tank (11), after-fractionating kettle (12), C receiving tank (13), D receiving tank (14), second cooling tower (15), second taper storage tank (16) and finished pot (17), exhaust gas cleaner includes water sealed tank (20) and chimney (21), the utility model advantage is：Purify mineral waste feedstock oil by second distillation more thorough, mineral waste feedstock oil and auxiliary agent carry out circulating-heating in the measuring tank and distillation still in reaction process twice respectively, are uniformly mixed liquid, improve and refine efficiency.
Description
Technical field
The utility model relates to technical field of petrochemical industry, and in particular to a kind of mineral waste feedstock oil refinement system.
Background technique
Currently, existing mineral waste feedstock oil extraction process is complicated, the utilization rate of mineral waste feedstock oil is not high, and waste residue is more,
Cause biggish waste.
Utility model content
For the purpose of this utility model aiming at currently, existing mineral waste feedstock oil extraction process is complicated, mineral waste is former
Expect that the utilization rate of oil is not high, waste residue is more, the deficiency of biggish waste is caused, and a kind of mineral waste feedstock oil refinement system is provided.
The utility model includes head tank, the first reaction storage device, the second reaction storage device and exhaust gas cleaner,
First reaction storage device includes the first measuring tank, the first auxiliary tank, the first distillation still, A receiving tank, B receiving tank, the first cooling
The liquid outlet of tower, the first taper storage tank and surge tank, head tank and the first auxiliary tank respectively with the inlet phase of the first measuring tank
Logical, the liquid outlet of the first measuring tank is communicated with the inlet of the first distillation still, the steam (vapor) outlet of the first distillation still and the first cooling
The air inlet of tower communicates, and the condensate outlet of the first cooling tower is communicated with the inlet of A receiving tank and B receiving tank respectively, and B is received
The liquid outlet of tank is communicated with the inlet of the first taper storage tank, the gas outlet of the first taper storage tank and the air inlet phase of surge tank
It is logical；Second reaction storage device includes the second measuring tank, the second auxiliary tank, after-fractionating kettle, C receiving tank, D receiving tank, second
The liquid outlet of cooling tower, the second taper storage tank and finished pot, A receiving tank and the second auxiliary tank feed liquor with the second measuring tank respectively
Mouth communicates, and the liquid outlet of the second measuring tank is communicated with the inlet of after-fractionating kettle, the steam (vapor) outlet of after-fractionating kettle and second
The air inlet of cooling tower communicates, and the condensate outlet of the second cooling tower is communicated with the inlet of C receiving tank and D receiving tank respectively, D
The liquid outlet of receiving tank is communicated with the inlet of the second taper storage tank, and the liquid outlet of C receiving tank is communicated with the inlet of finished pot；
Exhaust gas cleaner includes water sealed tank and chimney, and the gas outlet of surge tank and the second taper storage tank passes through vacuum pump and water seal respectively
It is communicated in tank, the gas outlet of water sealed tank is communicated with the air inlet of chimney；There are also a pair of of mixing liquid circulating devices and a pair of of oil to follow for it
Loop device, mixing liquid circulating device include heat exchange pump and heat exchanger, have mixing on the first measuring tank and the second measuring tank
Liquid circulation import and mixing liquid loop exit, the first measuring tank and the second measuring tank pass through corresponding heat exchange pump respectively and change
Circulation in hot device；Oil circulation device includes hot oil pump and heated beam, has circulation on the first distillation still and after-fractionating kettle
Oil inlet and circulation oil export, the first distillation still and after-fractionating kettle pass through circulation in corresponding hot oil pump and heated beam respectively.
The utility model advantage is：Mineral waste feedstock oil is set to purify more thorough, mineral waste feedstock oil by second distillation
Circulating-heating is carried out respectively in measuring tank of the auxiliary agent in reaction process twice and distillation still, is uniformly mixed liquid, is improved
Refine efficiency.
Detailed description of the invention
Fig. 1 is the utility model structure diagram.
Specific embodiment
As shown in the picture, the utility model include head tank 1, first react storage device, second reaction storage device and
Exhaust gas cleaner, the first reaction storage device includes the first measuring tank 2, the first auxiliary tank 3, the first distillation still 4, A receiving tank
5, the liquid outlet of B receiving tank 6, the first cooling tower 7, the first taper storage tank 8 and surge tank 9, head tank 1 and the first auxiliary tank 3 point
It not being communicated with the inlet of the first measuring tank 2, the liquid outlet of the first measuring tank 2 is communicated with the inlet of the first distillation still 4, and first
The steam (vapor) outlet of distillation still 4 is communicated with the air inlet of the first cooling tower 7, and the condensate outlet of the first cooling tower 7 is received with A respectively
Tank 5 and the inlet of B receiving tank 6 communicate, and the liquid outlet of B receiving tank 6 is communicated with the inlet of the first taper storage tank 8, the first cone
The gas outlet of shape storage tank 8 is communicated with the air inlet of surge tank 9；Second reaction storage device is helped including the second measuring tank 10, second
Agent tank 11, after-fractionating kettle 12, C receiving tank 13, D receiving tank 14, the second cooling tower 15, the second taper storage tank 16 and finished pot
The liquid outlet of 17, A receiving tanks 5 and the second auxiliary tank 11 is communicated with the inlet of the second measuring tank 10 respectively, the second measuring tank 10
Liquid outlet communicated with the inlet of after-fractionating kettle 12, the air inlet of the steam (vapor) outlet of after-fractionating kettle 12 and the second cooling tower 15
Mouth communicates, and the condensate outlet of the second cooling tower 15 is communicated with the inlet of C receiving tank 13 and D receiving tank 14 respectively, D receiving tank
14 liquid outlet is communicated with the inlet of the second taper storage tank 16, the inlet phase of the liquid outlet and finished pot 17 of C receiving tank 13
It is logical；Exhaust gas cleaner includes water sealed tank 20 and chimney 21, and the gas outlet of surge tank 9 and the second taper storage tank 16 passes through very respectively
Sky is pumped and is communicated in water sealed tank 20, and the gas outlet of water sealed tank 20 is communicated with the air inlet of chimney 21；There are also a pair of of mixed liquors to follow for it
Loop device and a pair of of oil circulation device, mixing liquid circulating device include heat exchange pump 22 and heat exchanger 23, the first measuring tank 2 and second
Mixing liquid circulation import and mixing liquid loop exit, the first measuring tank 2 and the second measuring tank are had on measuring tank 10
10 pass through circulation in corresponding heat exchange pump 22 and heat exchanger 23 respectively；Oil circulation device includes hot oil pump 24 and heated beam 25, and
Circulation oil inlet and circulation oil export, the first distillation still 4 and after-fractionating are had in one distillation still 4 and after-fractionating kettle 12
Kettle 12 passes through circulation in corresponding hot oil pump 24 and heated beam 25 respectively.
Working method principle：The auxiliary agent in mineral waste feedstock oil and the first auxiliary tank 3 in head tank 1 is respectively delivered to
In one measuring tank 2, then the mixed liquor in first measuring tank 2 is recycled and is heated up by heat exchange pump 22 and heat exchanger 23,
So that being uniformly mixed, enters in the first distillation still 4 and is distilled after circulation mixing, hot oil pump 24 and heated beam while distillation
Mixed liquor in 25 pair of first distillation still 4 carries out secondary cycle, is mixed by heated beam 25 to the liquid in the first distillation still 4
It closes and temperature controls, the gas after distillation is cooling by the first cooling tower 7, and condensate liquid enters in A receiving tank 5, A receiving tank 5
It enters in the second measuring tank 10 after being mixed and is distilled together with the auxiliary agent of the second auxiliary tank 11 again, mix and distill step
Suddenly identical as first time mixing distillation, the condensate liquid of second distillation enters in C receiving tank 13, then enters back into finished pot 17
Interior storage；In distillation process, the inlet of B receiving tank 6 and D receiving tank 14 is closed, and is being needed to the residual oil in the first distillation still 4
When cleaning, the hot oil pump 24 and heated beam 25 of the first distillation still 4 circulation are closed, the inlet of A receiving tank 5 is closed, B
The inlet of receiving tank 6 is opened, and the gas-liquid in the first cooling tower 7 enters in the first taper storage tank 8, in the first taper storage tank 8
Gas enter in surge tank 9, then the gas in surge tank 9 by vacuum pump be input in water sealed tank 20 filter after passes through cigarette
Chimney 21 discharges.Similarly when needing to clear up the residual oil in after-fractionating kettle 12, closes after-fractionating kettle 12 and recycle
Hot oil pump 24 and heated beam 25, the inlet of after-fractionating kettle 12 close, while the inlet of C receiving tank 13 is closed, and D is received
The inlet of tank 14 is opened, and the gas-liquid entered in D receiving tank 14 enters in the second taper storage tank 16, and gas is defeated by vacuum pump
It is discharged after entering into water sealed tank 20 filtering by chimney 21.
Claims (1)
1. a kind of mineral waste feedstock oil refines system, it is characterised in that it includes head tank (1), the first reaction storage device, the
Two reaction storage devices and exhaust gas cleaner, the first reaction storage device include the first measuring tank (2), the first auxiliary tank (3),
First distillation still (4), A receiving tank (5), B receiving tank (6), the first cooling tower (7), the first taper storage tank (8) and surge tank (9),
The liquid outlet of head tank (1) and the first auxiliary tank (3) is communicated with the inlet of the first measuring tank (2) respectively, the first measuring tank (2)
Liquid outlet communicated with the inlet of the first distillation still (4), the steam (vapor) outlet of the first distillation still (4) and the first cooling tower (7)
Air inlet communicates, and the condensate outlet of the first cooling tower (7) is communicated with the inlet of A receiving tank (5) and B receiving tank (6) respectively,
The liquid outlet of B receiving tank (6) is communicated with the inlet of the first taper storage tank (8), the gas outlet of the first taper storage tank (8) and buffering
The air inlet of tank (9) communicates；Second reaction storage device includes the second measuring tank (10), the second auxiliary tank (11), after-fractionating
Kettle (12), C receiving tank (13), D receiving tank (14), the second cooling tower (15), the second taper storage tank (16) and finished pot (17), A
The liquid outlet of receiving tank (5) and the second auxiliary tank (11) is communicated with the inlet of the second measuring tank (10) respectively, the second measuring tank
(10) liquid outlet is communicated with the inlet of after-fractionating kettle (12), the steam (vapor) outlet and the second cooling tower of after-fractionating kettle (12)
(15) air inlet communicates, the condensate outlet of the second cooling tower (15) respectively with C receiving tank (13) and D receiving tank (14) into
Liquid mouth communicates, and the liquid outlet of D receiving tank (14) is communicated with the inlet of the second taper storage tank (16), and C receiving tank (13) goes out liquid
Mouth is communicated with the inlet of finished pot (17)；Exhaust gas cleaner includes water sealed tank (20) and chimney (21), surge tank (9) and
The gas outlet of two taper storage tanks (16) passes through respectively to be communicated in vacuum pump and water sealed tank (20), the gas outlet of water sealed tank (20) and cigarette
The air inlet of chimney (21) communicates；It mixes liquid circulating device packet there are also a pair of of mixing liquid circulating device and a pair of of oil circulation device
Heat exchange pump (22) and heat exchanger (23) are included, mixing liquid circulation is had on the first measuring tank (2) and the second measuring tank (10)
Import and mixing liquid loop exit, the first measuring tank (2) and the second measuring tank (10) pass through corresponding heat exchange pump (22) respectively
With circulation in heat exchanger (23)；Oil circulation device includes hot oil pump (24) and heated beam (25), and the first distillation still (4) and second are steamed
It evaporates and has circulation oil inlet and circulation oil export on kettle (12), the first distillation still (4) and after-fractionating kettle (12) lead to respectively
Cross circulation in corresponding hot oil pump (24) and heated beam (25).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820524651.4U CN208104304U (en) | 2018-04-13 | 2018-04-13 | A kind of mineral waste feedstock oil refinement system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820524651.4U CN208104304U (en) | 2018-04-13 | 2018-04-13 | A kind of mineral waste feedstock oil refinement system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208104304U true CN208104304U (en) | 2018-11-16 |
Family
ID=64118428
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820524651.4U Expired - Fee Related CN208104304U (en) | 2018-04-13 | 2018-04-13 | A kind of mineral waste feedstock oil refinement system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208104304U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109468163A (en) * | 2018-04-13 | 2019-03-15 | 湖北爱国石化有限公司 | A kind of purification processing technology of mineral waste feedstock oil |
-
2018
- 2018-04-13 CN CN201820524651.4U patent/CN208104304U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109468163A (en) * | 2018-04-13 | 2019-03-15 | 湖北爱国石化有限公司 | A kind of purification processing technology of mineral waste feedstock oil |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105561616B (en) | A kind of gasification ash water low pressure flash heat-energy utilizing device and its heat energy utilization method | |
| CN204454584U (en) | Desulfurization waste liquor puies forward salt system | |
| CN102602960B (en) | Method for stilling ammonia by aid of waste heat of flue gas of coke oven and equipment | |
| CN110054164A (en) | A kind of dilute sulfuric acid system for concentrating and recycling | |
| CN208104304U (en) | A kind of mineral waste feedstock oil refinement system | |
| CN104709954A (en) | Ammonia stilling and desulfurating integrated system by utilizing waste heat of flue gas of coke oven | |
| CN105509027A (en) | Steam recycling device | |
| CN206739921U (en) | A kind of titanium white flour flow design air-flow crushing tail gas secondary waste heat recycling system | |
| CN205974481U (en) | Wine liquid heating evaporation system of cyclic utilization wine vapour heat energy | |
| CN105484716B (en) | Oil field produced liquid heat energy recovery device and method | |
| CN203947049U (en) | A kind of device of preparing formaldehyde | |
| CN208104305U (en) | A kind of mineral waste feedstock oil tentatively refines system | |
| CN205760487U (en) | A kind of yellow phosphoric tail gas absorption plant | |
| CN205115337U (en) | Low power consuming is by device of methyl alcohol preparation aerosol dimethyl ether | |
| CN204134245U (en) | A kind of flash distillation device | |
| CN108854456B (en) | System and method for recycling heat energy of desorption tower | |
| CN201906471U (en) | Vacuum concentration device for diluted acid | |
| CN204251370U (en) | Alcohol natural pond liquid deamination equipment | |
| CN102442884B (en) | Method for recovering ethanol during soy production process and device thereof | |
| CN104445476B (en) | Ethyl alcohol biogas slurry deamination technology and equipment | |
| CN203922752U (en) | A kind of device that removes ammonium sulfate and calcium carbonate mixture slurry free ammonia | |
| CN105886306A (en) | Wine liquid heating and evaporation system and method thereof with cyclic utilization of wine steam heat energy | |
| CN205556135U (en) | Vacuum environmental protection liquid waste processing system | |
| CN208170369U (en) | A kind of thermal energy of steam exhaust and the recyclable device of condensed water | |
| CN204897594U (en) | Area filtration and tail gas spray set's ageing liquid treatment facility of chemical nickel plating |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181116 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |