CN105647572B - A kind of proportion expression electromagnetic method heavy oil dehydration device - Google Patents
A kind of proportion expression electromagnetic method heavy oil dehydration device Download PDFInfo
- Publication number
- CN105647572B CN105647572B CN201610093381.1A CN201610093381A CN105647572B CN 105647572 B CN105647572 B CN 105647572B CN 201610093381 A CN201610093381 A CN 201610093381A CN 105647572 B CN105647572 B CN 105647572B
- Authority
- CN
- China
- Prior art keywords
- tank body
- ball float
- heavy oil
- main tank
- heating chamber
- 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.)
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- 239000000295 fuel oil Substances 0.000 title claims abstract description 55
- 230000018044 dehydration Effects 0.000 title claims abstract description 19
- 238000006297 dehydration reaction Methods 0.000 title claims abstract description 19
- 238000000034 method Methods 0.000 title claims abstract description 14
- 238000010438 heat treatment Methods 0.000 claims abstract description 69
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000003921 oil Substances 0.000 claims abstract description 11
- 238000009413 insulation Methods 0.000 claims abstract description 5
- 230000005674 electromagnetic induction Effects 0.000 claims description 7
- 238000010276 construction Methods 0.000 abstract description 4
- 208000005156 Dehydration Diseases 0.000 description 12
- 238000006243 chemical reaction Methods 0.000 description 5
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 230000009466 transformation Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G33/00—Dewatering or demulsification of hydrocarbon oils
- C10G33/02—Dewatering or demulsification of hydrocarbon oils with electrical or magnetic means
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- General Induction Heating (AREA)
- Drying Of Solid Materials (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The present invention relates to a kind of proportion expression electromagnetic method heavy oil dehydration device, including tank body, ball float drainage arrangement and heater, tank body includes main tank body, collecting chamber and heating chamber, collecting chamber is arranged on the upper end of main tank body, heating chamber is arranged on the lower end of main tank body, and collecting chamber and heating chamber are connected with main tank body, and the top of collecting chamber is provided with oil inlet, the bottom of heating chamber is provided with the heat-insulation layer for being additionally provided with and being close on its external wall outside oil-out, tank body；Ball float drainage arrangement includes ball float and scupper hose, and ball float is placed in tank body, and cavity is provided with ball float, and there is water inlet ball float upper end, one end of scupper hose is connected with the cavity of ball float, and the delivery port of the other end of scupper hose passes main tank body, and the density of ball float is between water and pure heavy oil.Compared with the prior art, simple in construction, simple to operate, cost of the invention is low, obtains heavy oil purity height, is adapted to various heavy oil dehydrating operations.
Description
Technical field
The present invention relates to heavy oil dehydration technique field, more particularly to a kind of proportion expression electromagnetic method heavy oil dehydration device.
Background technology
Heavy oil is unavoidable during processing, storage, transport and use to have moisture to enter wherein, in the prior art, every time oil
, it is necessary to which the Draw off valve for opening tank bottom is dehydrated when tank is dehydrated, inquire for that when being dehydrated a large amount of band oil dehydration could be stopped,
This simple traditional dewatering type often results in a large amount of band oil of dehydration, not only causes the loss of fuel oil, also effectively causes
The pollution of environment.This traditional dewatering type is used without corresponding system equipment.
The content of the invention
It is low that the technical problems to be solved by the invention are to provide a kind of simple in construction, simple to operate, cost, obtains heavy oil pure
Degree is high, is adapted to the proportion expression electromagnetic method heavy oil dehydration device of various heavy oil dehydrations.
The technical scheme that the present invention solves above-mentioned technical problem is as follows：A kind of proportion expression electromagnetic method heavy oil dehydration device, bag
Include tank body, ball float drainage arrangement and heater, the ball float drainage arrangement is placed in the tank body, the ball float drainage arrangement
The other end pass the tank body, the lower end heating that the heater is arranged on the tank body is outdoor.
Further, the tank body includes main tank body, collecting chamber and heating chamber, and the collecting chamber is arranged on the main tank body
Upper end, the heating chamber is arranged on the lower end of the main tank body, and the collecting chamber and heating chamber are connected with the main tank body,
The top of the collecting chamber is provided with oil inlet, and the bottom of the heating chamber, which is provided with outside oil-out, the tank body, to be additionally provided with
It is close to heat-insulation layer on its external wall.
Further, the heater includes rectification unit, inversion unit, control unit, resonance output unit and heater wire
Circle, the rectification unit, inversion unit, resonance output unit and heating coil are linked in sequence successively, described control unit and institute
Inversion unit connection is stated, the heating coil is around the heating chamber.
Further, it is provided with the thermally conductive sheet for being close to inwall in the heating chamber interior walls.
Further, the ratio between main tank body and the volume sum and the collecting chamber volume of heating chamber is equal to heavy oil reclaimed water
The ratio between with the volume of pure heavy oil.
Further, the heating coil is electromagnetic induction heating coil, the frequency of the electromagnetic induction heating coil power supply
For 10~14kHz.
Further, the temperature of the heating coils heat heavy oil is 70~80 DEG C.
Further, the ball float drainage arrangement includes ball float and scupper hose, and the ball float is placed in the tank body, described
Cavity is provided with ball float, and there is water inlet the ball float upper end, one end of the scupper hose and the cavity of the ball float connect
Logical, the delivery port of the other end of the scupper hose passes the main tank body, and the density of the ball float is between water and pure heavy oil.
The beneficial effects of the invention are as follows：
1st, the present apparatus is simple in construction, is easy to operation, and implementation cost is low, and is applicable various heavy oil dehydrations；
2nd, heater is electromagnetic induction heater, is medium-high frequency power supply by common power frequency supply frequency conversion, makes heating chamber by
High-frequency alternating magnetic field cutting, which is produced, to be vortexed and generates heat rapidly, high with heat conversion, and transformation efficiency reaches 95%, and power consumption is few, plus
The thermal efficiency is high；
3rd, heater is to the heavy-oil heating in tank body, after heavy oil and water separation, ball float drainage arrangement draining, drainage efficiency
Height, and be difficult to discharge heavy oil during draining；
4th, the oil-out discharge of heating chamber, obtains heavy oil purity high；
5th, the thermally conductive sheet for being close to inwall is provided with heating chamber interior walls, improves the heat conduction efficiency and heating effect of heating chamber
Really.
Brief description of the drawings
Fig. 1 is a kind of structural representation of proportion expression electromagnetic method heavy oil dehydration device of the invention；
Fig. 2 is the circuit theory diagrams of heater.
In accompanying drawing, the list of parts representated by each label is as follows：
1st, tank body, 11, heat-insulation layer, 12, collecting chamber, 13, heating chamber, 14, main tank body, 15, thermally conductive sheet；
2nd, ball float drainage arrangement, 21, ball float, 22, scupper hose；
3rd, heater, 31, rectification unit, 32, inversion unit, 33, control unit, 34, resonance output unit, 35, heating
Coil.
Embodiment
The principle and feature of the present invention are described below in conjunction with accompanying drawing, the given examples are served only to explain the present invention, and
It is non-to be used to limit the scope of the present invention.
As depicted in figs. 1 and 2, a kind of proportion expression electromagnetic method heavy oil dehydration device, including tank body 1, the and of ball float drainage arrangement 2
Heater 3, the ball float drainage arrangement 2 is placed in the tank body 1, and the other end of the ball float drainage arrangement 2 passes described
Tank body 1, the heater 3 is arranged on outside the lower end heating chamber 13 of the tank body 1.
The tank body 1 includes main tank body 14, collecting chamber 12 and heating chamber 13, and the collecting chamber 12 is arranged on the main tank body
14 upper end, the heating chamber 13 is arranged on the lower end of the main tank body (14), and the collecting chamber 12 and heating chamber 13 with
The main tank body 14 is connected, and the top of the collecting chamber 12 is provided with oil inlet, and the bottom of the heating chamber 13 is provided with fuel-displaced
Mouthful, it is additionally provided with the heat-insulation layer 11 being close on its external wall outside the tank body 1.
The heater 3 includes rectification unit 31, inversion unit 32, control unit 33, resonance output unit 34 and heating
Coil 35, the rectification unit 31, inversion unit 32, resonance output unit 34 and heating coil 35 are linked in sequence successively, described
Control unit 33 is connected with the inversion unit 32, and the heating coil 35 is around the heating chamber 13.
The thermally conductive sheet 15 for being close to inwall is provided with the inwall of heating chamber 13.
Ratio between main tank body 14 and the volume sum and the volume of the collecting chamber 12 of heating chamber 13 is equal to heavy oil reclaimed water
The ratio between with the volume of pure heavy oil.
The heating coil 35 is electromagnetic induction heating coil, the frequency of the electromagnetic induction heating coil power supply for 10~
14kHz。
The temperature of the heating heavy oil of heating coil 35 is 70~80 DEG C.
The ball float drainage arrangement 2 includes ball float 21 and scupper hose 22, and the ball float 21 is placed in the tank body 1, institute
State and cavity is provided with ball float 21, and there are water inlet, one end and the ball float of the scupper hose 22 in the upper end of the ball float 21
21 cavity connection, the delivery port of the other end of the scupper hose 22 passes the main tank body 11, and the density of the ball float exists
Between water and pure heavy oil.
Heavy oil is added into tank body 1 from the oil inlet of collecting chamber 12, oil is expired to collecting chamber 3/5ths；Use heater
3 pairs of heating chambers 13 are heated, and make the profit in heavy oil because proportion difference is separated, main tank body 11 and heating chamber are sunk under pure heavy oil
It is waterborne to float in collecting chamber 12 in 13；Ball float 21 is floated up on the interface between the water after separation and pure heavy oil, opens draining
The delivery port of flexible pipe 22, the water in the top of ball float 21 flows into the water inlet of ball float 21, passes through the outwardly draining of scupper hose 22；It is de-
The oil-out discharge of the heated room 13 of heavy oil after water.
The power frequency three-phase alternating current of outside access is converted into DC voltage by rectification unit 31；Control unit 33 controls inverse
Become unit 32 by DC power conversion into high-frequency alternating current；High-frequency alternating current is transformed into by resonance output unit 34 using resonance principle
High frequency electric；Heating coil 35 is passed through high frequency electric and produces high-frequency alternating magnetic field, and high-frequency alternating magnetic field cutting heating chamber 13 is produced
It is vortexed and generates heat rapidly and heating chamber 13 is heated.
Present apparatus operation principle：Heavy oil is added into tank body 1 to the oil inlet of collecting chamber 12, heater 3 is to heating chamber 13
Heated, heater 3 is to the heavy-oil heating in heating chamber 13 to 70~80 DEG C, and heavy oil is after static, and water is separated from heavy oil
Collecting chamber 12 is out rested on, heavy oil is deposited in main tank body 11 and heating chamber 13, and ball float 21 is suspended into the boundary of heavy oil and water
On face, water more than interface enters from the discharge outlet on ball float 21, and water is drained to outside by the water conservancy diversion through scupper hose 22,
Realize heavy oil success draining.
The present apparatus is simple in construction, is easy to operation, and implementation cost is low, and is applicable various heavy oil dehydrations；Heater 3 is electromagnetism sense
Heater is answered, is medium-high frequency power supply by common power frequency supply frequency conversion, heating chamber 13 is produced whirlpool by the cutting of medium-high frequency alternating magnetic field
Flow and generate heat rapidly, high with heat conversion, transformation efficiency reaches 95%, and power consumption is few, and the efficiency of heating surface is high；Heater 3 is to tank body 1
In heavy-oil heating, after heavy oil and water separation, the drainage arrangement draining of ball float 21, drainage efficiency is high, and discharge weight is difficult during draining
Oil；The oil-out discharge heavy oil of heating chamber 13, obtains heavy oil purity high.
The foregoing is only presently preferred embodiments of the present invention, be not intended to limit the invention, it is all the present invention spirit and
Within principle, any modification, equivalent substitution and improvements made etc. should be included in the scope of the protection.
Claims (5)
1. a kind of proportion expression electromagnetic method heavy oil dehydration device, it is characterised in that：Including tank body (1), ball float drainage arrangement (2) and add
Hot device (3), the tank body (1) includes main tank body (14), collecting chamber (12) and heating chamber (13), and the collecting chamber (12) is arranged on
The upper end of the main tank body (14), the heating chamber (13) is arranged on the lower end of the main tank body (14), and the collecting chamber
(12) connected with heating chamber (13) with the main tank body (14), the top of the collecting chamber (12) is provided with oil inlet, described
The bottom of heating chamber (13) is provided with outside oil-out, the tank body (1) and is additionally provided with the heat-insulation layer (11) being close on its external wall；
The ball float drainage arrangement (2) includes ball float (21) and scupper hose (22), and the ball float (21) is placed in the tank body (1)
It is interior, cavity is provided with the ball float (21), and there are water inlet, one end of the scupper hose (22) in the ball float (21) upper end
Connected with the cavity of the ball float (21), the delivery port of the other end of the scupper hose (22) passes the main tank body (11),
The density of the ball float is between water and pure heavy oil；The heater (3) includes rectification unit (31), inversion unit (32), control
Unit (33) processed, resonance output unit (34) and heating coil (35), the rectification unit (31), inversion unit (32), resonance
Output unit (34) and heating coil (35) are linked in sequence successively, and described control unit (33) connects with the inversion unit (32)
Connect, the heating coil (35) is around the heating chamber (13).
2. a kind of proportion expression electromagnetic method heavy oil dehydration device according to claim 1, it is characterised in that：The heating chamber (13)
The thermally conductive sheet (15) for being close to inwall is provided with inwall.
3. a kind of proportion expression electromagnetic method heavy oil dehydration device according to claim 1, it is characterised in that：Main tank body (14) and add
Ratio between the volume sum and the collecting chamber (12) volume in hot cell (13) be equal to heavy oil reclaimed water and pure heavy oil volume it
Than.
4. a kind of proportion expression electromagnetic method heavy oil dehydration device according to claim 2, it is characterised in that：The heating coil
(35) it is electromagnetic induction heating coil, the frequency of the electromagnetic induction heating coil power supply is 10~14kHz.
5. a kind of proportion expression electromagnetic method heavy oil dehydration device according to claim 4, it is characterised in that：The heating coil
(35) temperature of heating heavy oil is 70~80 DEG C.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710641806.2A CN107267196B (en) | 2016-02-19 | 2016-02-19 | A kind of working method of proportion expression electromagnetic method heavy oil dehydration device |
| CN201610093381.1A CN105647572B (en) | 2016-02-19 | 2016-02-19 | A kind of proportion expression electromagnetic method heavy oil dehydration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610093381.1A CN105647572B (en) | 2016-02-19 | 2016-02-19 | A kind of proportion expression electromagnetic method heavy oil dehydration device |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710641806.2A Division CN107267196B (en) | 2016-02-19 | 2016-02-19 | A kind of working method of proportion expression electromagnetic method heavy oil dehydration device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105647572A CN105647572A (en) | 2016-06-08 |
| CN105647572B true CN105647572B (en) | 2017-10-27 |
Family
ID=56488496
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710641806.2A Active CN107267196B (en) | 2016-02-19 | 2016-02-19 | A kind of working method of proportion expression electromagnetic method heavy oil dehydration device |
| CN201610093381.1A Active CN105647572B (en) | 2016-02-19 | 2016-02-19 | A kind of proportion expression electromagnetic method heavy oil dehydration device |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710641806.2A Active CN107267196B (en) | 2016-02-19 | 2016-02-19 | A kind of working method of proportion expression electromagnetic method heavy oil dehydration device |
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| Country | Link |
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| CN (2) | CN107267196B (en) |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2321990A1 (en) * | 1998-02-27 | 1999-09-02 | Masanori Itakura | Crude oil processing apparatus and crude oil processing method |
| CN2464729Y (en) * | 2001-01-20 | 2001-12-12 | 长江(扬中)电脱盐设备公司 | High-speed electric desalinating and dewatering equipment |
| CN101178250B (en) * | 2007-11-29 | 2010-09-29 | 江南大学 | Induction heating rapid water heater |
| CN202246582U (en) * | 2011-10-28 | 2012-05-30 | 中国海洋石油总公司 | Crude oil dehydration device |
| CN104046379B (en) * | 2013-03-12 | 2015-12-09 | 中石化洛阳工程有限公司 | A kind of heavy oil storage tank dewatering unit |
| WO2015180873A1 (en) * | 2014-05-28 | 2015-12-03 | Basf Se | Coated mesh and its use for oil-water separation |
-
2016
- 2016-02-19 CN CN201710641806.2A patent/CN107267196B/en active Active
- 2016-02-19 CN CN201610093381.1A patent/CN105647572B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN105647572A (en) | 2016-06-08 |
| CN107267196A (en) | 2017-10-20 |
| CN107267196B (en) | 2019-07-30 |
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Legal Events
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Qiu Youzhang Inventor before: Lv Zhiqiang |
|
| TA01 | Transfer of patent application right | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20170725 Address after: 330114 Jiangxi city of Nanchang province Xinjian County Lehua Zhen Lao Wu Cun Xia Fang Village No. 7 1 Applicant after: Qiu Youzhang Address before: 541100, Guilin, Lingui County, the Guangxi Zhuang Autonomous Region County Xinmin Village village, Ma Tau Village, No. 63-1 Applicant before: Lv Zhiqiang |
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| TA01 | Transfer of patent application right |
Effective date of registration: 20170912 Address after: 401320 Chongqing city Banan District Road No. 26 department in Baxian Fortune Tower No. 13-13 Applicant after: Chongqing days Spring Technology Co.,Ltd. Address before: 330114 Jiangxi city of Nanchang province Xinjian County Lehua Zhen Lao Wu Cun Xia Fang Village No. 7 1 Applicant before: Qiu Youzhang |
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| TR01 | Transfer of patent right |
Effective date of registration: 20180112 Address after: Chongqing city Banan District 401347 Zhen TA Nan Luo Cun Peng Yang Gang Group No. 41 Patentee after: Li Daibi Address before: 401320 Chongqing city Banan District Road No. 26 department in Baxian Fortune Tower No. 13-13 Patentee before: Chongqing days Spring Technology Co.,Ltd. |
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| CP02 | Change in the address of a patent holder | ||
| CP02 | Change in the address of a patent holder |
Address after: 313000 west side of Waihuan West Road, Yangnan village, Nanxun Economic Development Zone, Huzhou City, Zhejiang Province Patentee after: Li Daibi Address before: Chongqing city Banan District 401347 Zhen TA Nan Luo Cun Peng Yang Gang Group No. 41 Patentee before: Li Daibi |
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Effective date of registration: 20221114 Address after: 414009 Floor 4, Building 21, Changlian Chaoyang Village, Yunxi District, Yueyang City, Hunan Province Patentee after: Hunan Zhonglian Petrochemical Equipment Inspection and Maintenance Co.,Ltd. Address before: 313000 west side of Waihuan West Road, Yangnan village, Nanxun Economic Development Zone, Huzhou City, Zhejiang Province Patentee before: Li Daibi |