CN105733665B - One kind removal of impurities heavy oil dehydration device - Google Patents
One kind removal of impurities heavy oil dehydration device Download PDFInfo
- Publication number
- CN105733665B CN105733665B CN201610093278.7A CN201610093278A CN105733665B CN 105733665 B CN105733665 B CN 105733665B CN 201610093278 A CN201610093278 A CN 201610093278A CN 105733665 B CN105733665 B CN 105733665B
- Authority
- CN
- China
- Prior art keywords
- tank body
- heavy oil
- main tank
- ball float
- 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 56
- 230000018044 dehydration Effects 0.000 title claims abstract description 19
- 238000006297 dehydration reaction Methods 0.000 title claims abstract description 19
- 239000012535 impurity Substances 0.000 title claims abstract description 15
- 238000010438 heat treatment Methods 0.000 claims abstract description 72
- 239000003921 oil Substances 0.000 claims abstract description 11
- 238000009413 insulation Methods 0.000 claims abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 230000005674 electromagnetic induction Effects 0.000 claims description 6
- 238000010276 construction Methods 0.000 abstract description 4
- 238000000338 in vitro Methods 0.000 abstract 1
- 208000005156 Dehydration Diseases 0.000 description 11
- 238000006243 chemical reaction Methods 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- BGPVFRJUHWVFKM-UHFFFAOYSA-N N1=C2C=CC=CC2=[N+]([O-])C1(CC1)CCC21N=C1C=CC=CC1=[N+]2[O-] Chemical compound N1=C2C=CC=CC2=[N+]([O-])C1(CC1)CCC21N=C1C=CC=CC1=[N+]2[O-] BGPVFRJUHWVFKM-UHFFFAOYSA-N 0.000 description 3
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000000034 method 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
- C10G53/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes
- C10G53/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes plural serial stages only
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/208—Sediments, e.g. bottom sediment and water or BSW
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)
Abstract
The present invention relates to one kind removal of impurities heavy oil dehydration device, including tank body, ball float drainage arrangement and heater, the tank body includes main tank body, collecting chamber and heating chamber, the collecting chamber is arranged on the upper end of the main tank body, the heating chamber is arranged on the lower end of the main tank body, and the collecting chamber and heating chamber connect with the main tank body, the top of the collecting chamber is provided with oil inlet, the bottom of the heating chamber is provided with oil-out, and the main tank is additionally provided with the heat-insulation layer being close on its external wall in vitro；The bottom of the heating chamber is additionally provided with permanent magnet, and the permanent magnet is annularly in the Wai Yiquan of the oil-out.Compared with the prior art, the present invention is simple in construction, simple to operate, cost is low, obtains heavy oil purity height, is adapted to various heavy oil dehydrating operations, and can effectively clean.
Description
Technical field
The present invention relates to heavy oil dehydration technique field, more particularly to a kind of removal of impurities heavy oil dehydration device.
Background technology
Heavy oil has moisture to enter wherein unavoidably during processing, storage, transport and use, in the prior art, each oil
, it is necessary to the Draw off valve for opening tank bottom is dehydrated when tank is dehydrated, inquire for being dehydrated largely with it is oily when could stop being dehydrated,
This simple traditional dewatering type often results in dehydration largely band oil, not only causes the loss of fuel oil, also effectively causes
The pollution of environment.This traditional dewatering type uses without corresponding system equipment.
The content of the invention
The technical problems to be solved by the invention be to provide it is a kind of it is simple in construction, simple to operate, cost is low, it is pure to obtain heavy oil
Degree is high, is adapted to various heavy oil dehydrations, and the removal of impurities heavy oil dehydration device that can effectively clean.
The technical scheme that the present invention solves above-mentioned technical problem is as follows：One kind removal of impurities heavy oil dehydration device, including it is tank body, floating
Ball drainage arrangement and heater, the ball float drainage arrangement are placed in the tank body, the other end of the ball float drainage arrangement
The tank body is passed, the heater is arranged on outside the lower end heating chamber of the tank body.
The tank body includes main tank body, collecting chamber and heating chamber, and the collecting chamber is arranged on the upper end of the main tank body, institute
The lower end that heating chamber is arranged on the main tank body is stated, and the collecting chamber and heating chamber connect with the main tank body, the collection
The top of hydroecium is provided with oil inlet, and the bottom of the heating chamber is provided with oil-out, and the main tank is additionally provided with vitro to be close to
Heat-insulation layer on its external wall；
The bottom of the heating chamber is additionally provided with permanent magnet, and the permanent magnet is annularly in the oil-out
Wai Yiquan.
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 the volume sum and the collecting chamber volume of main tank body and 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, 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 produces, to be vortexed and generates heat rapidly, has heat conversion height, and transformation efficiency reaches 95%, and power consumption is few, adds
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, and drainage efficiency
Height, and be not easy to discharge heavy oil during draining；
4th, the oil-out discharge of heating chamber, it is high to obtain heavy oil purity；
5th, heat in chamber interior walls and be provided with the thermally conductive sheet for being close to inwall, improve the heat conduction efficiency and heating effect of heating chamber
Fruit；
6th, permanent magnet can clean, while can effectively prevent out to the iron impurity at oil-out to heavy oil
Hydraulic fluid port blocks.
Brief description of the drawings
Fig. 1 is a kind of structural representation for the heavy oil dehydration device that cleans of the present 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；
4th, permanent magnet.
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 removal of impurities heavy oil dehydration device, including tank body 1, ball float drainage arrangement 2 and 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 the tank body 1, institute
Heater 3 is stated to be 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 are arranged on the lower end of the main tank body 14, and the collecting chamber 12 and heating chamber 13 are and institute
Main tank body 14 to be stated to connect, the top of the collecting chamber 12 is provided with oil inlet, and the bottom of the heating chamber 13 is provided with oil-out,
The heat-insulation layer 11 being close on its external wall is additionally provided with outside the main tank body 14；
The bottom of the heating chamber 13 is additionally provided with permanent magnet 4, and the permanent magnet 4 annularly goes out described in
The Wai Yiquan of hydraulic fluid port.
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 the volume sum and the volume of the collecting chamber 12 of main tank body 14 and 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 pass 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 heat, and the profit in heavy oil is separated because proportion is different, sink to main tank body 11 and heating chamber 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 above ball float 21 flow into the water inlet of ball float 21, pass 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 produces
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 after static, water separates heavy oil 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, the water conservancy diversion through scupper hose 22, water is drained into outside,
Realize heavy oil success draining.
The present apparatus is simple in construction, 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 cut by medium-high frequency alternating magnetic field and produces whirlpool
Flow and generate heat rapidly, have heat conversion high, transformation efficiency reaches 95%, consumes energy few, 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 not easy during draining
Oil；The oil-out discharge heavy oil of heating chamber 13, it is high to obtain heavy oil purity；Permanent magnet 4 can to the iron impurity at oil-out,
Heavy oil can be cleaned, while effectively can prevent oil-out from blocking.
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., it should be included in the scope of the protection.
Claims (6)
1. one kind removal of impurities heavy oil dehydration device, it is characterised in that：Including tank body (1), ball float drainage arrangement (2) and heater (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 main tank
The upper end of body (14), the heating chamber (13) are arranged on the lower end of the main tank body (14), and the collecting chamber (12) and heating
Room (13) connects with the main tank body (14), and the top of the collecting chamber (12) is provided with oil inlet, the heating chamber (13)
Bottom be provided with oil-out, be additionally provided with the heat-insulation layer (11) being close on its external wall outside the main tank body (14)；
The bottom of the heating chamber (13) is additionally provided with permanent magnet (4), and the permanent magnet (4) is annularly in described
The Wai Yiquan of oil-out；
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
Being 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.
A kind of 2. removal of impurities heavy oil dehydration device according to claim 1, it is characterised in that：The heater (3) includes rectification
Unit (31), inversion unit (32), control unit (33), resonance output unit (34) and heating coil (35), the rectification list
First (31), inversion unit (32), resonance output unit (34) and heating coil (35) are linked in sequence successively, described control unit
(33) it is connected with the inversion unit (32), the heating coil (35) is around the heating chamber (13).
A kind of 3. removal of impurities heavy oil dehydration device according to claim 1, it is characterised in that：Set on heating chamber (13) inwall
It is equipped with the thermally conductive sheet (15) for being close to inwall.
A kind of 4. removal of impurities heavy oil dehydration device according to claim 1, it is characterised in that：Main tank body (14) and heating chamber (13)
Volume sum and the collecting chamber (12) volume between ratio be equal to the ratio between volume of heavy oil reclaimed water and pure heavy oil.
A kind of 5. removal of impurities heavy oil dehydration device according to claim 2, it is characterised in that：The heating coil (35) is electromagnetism
Load coil, the frequency of the electromagnetic induction heating coil power supply is 10~14kHz.
A kind of 6. removal of impurities heavy oil dehydration device according to claim 5, it is characterised in that：Heating coil (35) the heating weight
The temperature of oil is 70~80 DEG C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610093278.7A CN105733665B (en) | 2016-02-19 | 2016-02-19 | One kind removal of impurities heavy oil dehydration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610093278.7A CN105733665B (en) | 2016-02-19 | 2016-02-19 | One kind removal of impurities heavy oil dehydration device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105733665A CN105733665A (en) | 2016-07-06 |
| CN105733665B true CN105733665B (en) | 2017-11-14 |
Family
ID=56246039
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610093278.7A Active CN105733665B (en) | 2016-02-19 | 2016-02-19 | One kind removal of impurities heavy oil dehydration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105733665B (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
-
2016
- 2016-02-19 CN CN201610093278.7A patent/CN105733665B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN105733665A (en) | 2016-07-06 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20170829 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: 20170913 Address after: 401344 Chongqing District of Banan City Shilong Town Dalian Village Dragon Tsui Group No. 114 Applicant after: Chongqing wonderful biological science and 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 |
|
| TA01 | Transfer of patent application right | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Xue Guanglin Inventor after: Xue Mingwei Inventor after: Wang Jianyou Inventor before: Qiu Youzhang |
|
| TA01 | Transfer of patent application right | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20171010 Address after: The high-tech economic zone 224700 Jiangsu province Yancheng City Jianhu County Tang Qiao Lu 888 Applicant after: Yancheng Ruide Petrochemical Machinery Co., Ltd. Address before: 401344 Chongqing District of Banan City Shilong Town Dalian Village Dragon Tsui Group No. 114 Applicant before: Chongqing wonderful biological science and Technology Co Ltd |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: A device for removing impurities and dehydrating heavy oil Effective date of registration: 20201215 Granted publication date: 20171114 Pledgee: Bank of China Limited Jianhu Branch Pledgor: YANCHENG RUIDE PETROCHEMICAL MACHINERY Co.,Ltd. Registration number: Y2020320000246 |