CN106190210A - Coal tar product deployment device - Google Patents
Coal tar product deployment device Download PDFInfo
- Publication number
- CN106190210A CN106190210A CN201610619064.9A CN201610619064A CN106190210A CN 106190210 A CN106190210 A CN 106190210A CN 201610619064 A CN201610619064 A CN 201610619064A CN 106190210 A CN106190210 A CN 106190210A
- Authority
- CN
- China
- Prior art keywords
- groove
- distributing groove
- heat exchanger
- exchanger tube
- distributing
- 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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Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
- C10C3/00—Working-up pitch, asphalt, bitumen
- C10C3/005—Working-up pitch, asphalt, bitumen by mixing several fractions (also coaltar fractions with petroleum fractions)
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L95/00—Compositions of bituminous materials, e.g. asphalt, tar, pitch
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
- C10C1/00—Working-up tar
- C10C1/04—Working-up tar by distillation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
- F28B1/02—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using water or other liquid as the cooling medium
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Civil Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses and provide a kind of coal tar product deployment device, including tar distillation device, Colophonium chiller, heavy oil groove, the first distributing groove, the second distributing groove, vertical lower resistance cooling system, cooling back installation, finished product oil groove and scrubbing tower.Thus, enter back into scrubbing tower through overcooled blue or green cigarette and wash, reduce environmental pollution.Additionally, the first agitator, the second agitator, the first temperature sensing device, the second temperature sensing device set up so that whole system energy continuous and automatic is carried out, improve further allotment efficiency, it is ensured that product quality.
Description
Technical field
The present invention relates to coal tar processing field, particularly to coal tar product deployment device.
Background technology
During coal tar processing, the mid temperature pitch of general generation about about 55%, belongs to the bulk product of tar production,
Process scale is the biggest, and yield is the most.Mid temperature pitch can be used for producing modified coal tar pitch, if but substantial amounts of Colophonium only produces modification drip
Green grass or young crops, often restriction tar production produces.Oil product preparation is the way solving Colophonium outlet, with becoming of Colophonium and carbolineum mixture
Product oil may be used for producing fuel oil, carbon black oil or asphaltum oil export trade.The most at home during coal tar processing, oil product preparation
It is all with the various oil products produced in Process of Tar Processing and Colophonium, carries out in the make-up tank of atmospheric vertical flat cover belt stirrer
Mixture, Batch Process.According to the method, the Colophonium that tar distillation comes is directly placed in make-up tank, during stirring
Be gradually added into the tarry distillates such as carbolineum, its add number depending on product requirement, owing to asphalt temperature is the highest, add carbolineum
During oil product, there is the substantial amounts of bitumen flue gas with heat to evaporate, and the blue or green cigarette of heat has a strong impact on asking of environment
Topic.
Summary of the invention
For solving the one or more of the problems referred to above, it is provided that the coal tar product deployment device of a kind of environmental protection.
According to an aspect of the invention, it is provided a kind of coal tar product deployment device, including tar distillation device, drip
Blue or green chiller, heavy oil groove, the first distributing groove, the second distributing groove, vertical lower resistance cooling system, cooling back installation, one-tenth
Product oil groove and scrubbing tower, tar distillation device and Colophonium chiller are by pipeline communication, and Colophonium chiller and first is joined
Oil groove passes through pipeline communication, heavy oil groove and the first distributing groove and passes through pipeline communication, and the first distributing groove and the second distributing groove pass through
Pipeline communication, the second distributing groove and finished product oil groove are by pipeline communication, and the first distributing groove top has the first exhanst gas outlet, and second
Distributing groove top has the second exhanst gas outlet, and vertical lower resistance cooling system includes shell body and the heat exchange being fixed in shell body
Pipe, shell body top offers passage, and shell body bottom is provided with condensation-water drain, and shell body side is provided with hot air intake, changes
Heat pipe outer wall has some wire bending heat exchanging piece along longitudinal measure, and heat exchanger tube is respectively arranged at two ends with refrigerant inlet and refrigeration up and down
Agent exports, and refrigerant inlet connects with cooling back installation respectively with refrigerant outlet, and the first exhanst gas outlet and the second flue gas go out
Mouth is connected with hot air intake by pipeline respectively, and vertical lower resistance cooling system connects with scrubbing tower.It provides the benefit that: due to
The blue or green flue gas body of heat is little through vertical the be hampered power of lower resistance Cold cutting systems, is changed by heat exchanger tube with intermittent fever green grass or young crops flue gas body
Heat, steam meets cold liquefaction, owing to this vertical lower resistance cooling system is disposed vertically, therefore condensed water under gravity vertically to
Under flow out to wastewater disposal basin, thus, greatly reduce the waste of water resource and the pollution to environment, again through overcooled blue or green cigarette simultaneously
Enter scrubbing tower to wash, reduce environmental pollution.
In some embodiments, heat exchanger tube is hollow copper tubing, and wire bending heat exchanging piece is the copper wire of bending, every copper wire
All it is welded in the outer tube wall of hollow copper tubing after two ends bending from beginning to end, and adjacent two copper wires of each row interlock superposition.It is useful
Effect is: the copper wire of this structure, this permutation and combination method substantially increase between copper wire and heat exchanger tube connect compactness,
Fastness and stability, improve its service life, is simultaneously also beneficial to the conduction of heat.Additionally can increase heat exchanger tube
Transmission of heat by contact area with heat smoke so that heat transfer effect further enhances, and heat exchange efficiency is higher, heat exchanger tube is more preferable, and copper
Silk bending heat exchanging piece makes simple；By making to be connected more firm with cooling tube welding, thus copper wire is difficult to from cooling tube
Get loose.
In some embodiments, also including multiple copper coil, copper coil welds along the outer tube wall longitudinal direction of heat exchanger tube,
Each copper coil is welded as a whole along the radial direction of heat exchanger tube with the first copper wire.It provides the benefit that: copper coil is along the footpath of heat exchanger tube
It is welded as a whole to the first copper wire, so that copper wire, copper coil and heat exchanger tube are collectively forming one stable is difficult to deformation
Entirety, and outside defines network structure, and inner side forms a plurality of axial passage, increases heat exchange area, is conducive to heat empty
The entrance of gas, and the outflow of condensed water.It addition, heat exchanger tube, copper wire, coil are welded together by the way of welding
Words, it is ensured that the steadiness of connection, and it is greatly saved production cost.
In some embodiments, the first compression pump it is provided with between heavy oil groove and the first distributing groove.It provides the benefit that:
Mink cell focus in heavy oil groove is beneficially transported in the first distributing groove by being provided with of the first compression pump.
In some embodiments, the second compression pump it is provided with between the second distributing groove and finished product oil groove.It provides the benefit that:
Oil in first distributing groove is beneficially transported in the second distributing groove by being provided with of the second compression pump.
Accompanying drawing explanation
Fig. 1 is the structural representation of the coal tar product deployment device of an embodiment of the present invention；
Fig. 2 is the structural representation of vertical cooling system shown in Fig. 1.
Detailed description of the invention
1 and 2 the present invention is further detailed explanation below in conjunction with the accompanying drawings.
Fig. 1 show schematically show the coal tar product deployment device according to one embodiment of the present invention, including Jiao
Oil distilling apparatus 1, Colophonium chiller 2, heavy oil groove the 3, first distributing groove the 4, second distributing groove 5, vertical lower resistance cooling system
System 7, cooling back installation 8, finished product oil groove 6 and scrubbing tower 13, tar distillation device 1 and Colophonium chiller 2 pass through pipeline
Connection, Colophonium chiller 2 and the first distributing groove 4 are by pipeline communication, and heavy oil groove 3 and the first distributing groove 4 are by pipeline even
Logical, the first distributing groove 4 and the second distributing groove 5 pass through pipeline communication by pipeline communication, the second distributing groove 5 with finished product oil groove 6, the
One distributing groove 4 top has the first exhanst gas outlet 401, and the second distributing groove 5 top has the second exhanst gas outlet 501, vertical low-resistance
Power cooling system 7 includes shell body 701 and the heat exchanger tube 703 being fixed in shell body 701, and shell body 701 top offers logical
Pore 705, shell body 701 bottom is provided with condensation-water drain 708, and shell body 701 side is provided with hot air intake 702, heat exchanger tube 703
Outer wall has some wire bending heat exchanging piece 704 along longitudinal measure, and heat exchanger tube about 703 is respectively arranged at two ends with refrigerant inlet 707
With refrigerant outlet 706, in heat exchanger tube 703, there are cold-producing medium, refrigerant inlet 707 and refrigerant outlet 706 cold with circulation respectively
Radiator cooler 8 connects to ensure the cooling effect of cold-producing medium, and the first exhanst gas outlet 401 and the second exhanst gas outlet 501 are respectively by pipe
Road connects with hot air intake 702, and vertical lower resistance cooling system 7 connects with scrubbing tower 13.Oil mixing is joined more in order to allow
Uniformly, oil product effect is more preferable, can be provided with the first agitator 11, be provided with second and stir in the second distributing groove 5 in the first distributing groove 4
Mixing device 12, the first distributing groove 4 outer wall is provided with first and adds heat pipe 402 and the first temperature sensing device, and the second distributing groove 5 outer wall is provided with
Second adds heat pipe 502 and the second temperature sensing device, first agitator the 11, second agitator the 12, first temperature sensing device,
Two stability induction installations, first add heat pipe 402 and second and add heat pipe 502 and be all connected with controller.Controller controls first and stirs
Mixing mixing speed and the mixing time of device the 11, second agitator 12, controller is also by the first temperature sensing device and second
Stability induction installation feeds back the temperature data come, and control first adds heat pipe 402 and second and adds the heating state of heat pipe 502.By
Little through vertical the be hampered power of lower resistance Cold cutting systems in the blue or green flue gas body of heat, entered by heat exchanger tube 703 with intermittent fever green grass or young crops flue gas body
Row heat exchange, the steam cold liquefaction of chance, owing to this vertical lower resistance cooling system 7 is disposed vertically, therefore condensed water is under gravity
Flow out to wastewater disposal basin vertically downward, can recycle further, thus, greatly reduce the waste of water resource and to ring
The pollution in border, enters back into scrubbing tower 13 through overcooled blue or green cigarette simultaneously and washs, reduce environmental pollution.Additionally, the first stirring
Device the 11, second agitator the 12, first temperature sensing device, the second temperature sensing device, first add heat pipe 402 and the second heating
Pipe 502 and controller set up so that whole system energy continuous and automatic is stirred, heats up, improve allotment efficiency further,
Ensure product quality.
Preferably, heat exchanger tube 703 is hollow copper tubing, and wire bending heat exchanging piece 704 is the copper wire 7041 of bending, every copper wire
All it is welded in the outer tube wall of hollow copper tubing after 7041 head and the tail two ends bendings, and adjacent two copper wires 7041 of each row are staggered folded
Add.It provides the benefit that: the copper wire 7041 of this structure, and this permutation and combination method substantially increases copper wire 7041 and heat exchanger tube
Compactness, fastness and the stability connected between 703, improves its service life, is simultaneously also beneficial to the conduction of heat.
Additionally can increase the transmission of heat by contact area of heat exchanger tube 703 and heat smoke so that heat transfer effect further enhances, heat exchange efficiency
Higher, heat exchanger tube 703 is more preferable, and copper wire 7041 bending heat exchanging piece makes simple；By making to be connected more with cooling tube welding
Add firm, thus copper wire 7041 is difficult to get loose from cooling tube.
Preferably, also including multiple copper coil 7042, copper coil 7042 welds along the outer tube wall longitudinal direction of heat exchanger tube 703
Connecing, each copper coil 7042 is welded as a whole along the radial direction of heat exchanger tube 703 with the first copper wire 7041.It provides the benefit that: copper cash
Circle 7042 is welded as a whole along the radial direction of heat exchanger tube 703 with the first copper wire 7041, so that copper wire 7041, copper coil 7042 and
Heat exchanger tube 703 is collectively forming the stable entirety being difficult to deformation, and outside defines network structure, and inner side is formed a plurality of
Axial passage, increases heat exchange area, the outflow of the beneficially entrance of hot-air, and condensed water.It addition, by the side of welding
If heat exchanger tube 703, copper wire 7041, coil are welded together by formula, it is ensured that the steadiness of connection, and it is greatly saved production
Cost.
Preferably, it is provided with the first compression pump 9 between heavy oil groove 3 and the first distributing groove 4.It provides the benefit that: the first pressure
Mink cell focus in heavy oil groove 3 is beneficially transported in the first distributing groove 4 by being provided with of power pump 9.
Preferably, the second compression pump 10 it is provided with between the second distributing groove 5 and finished product oil groove 6.It provides the benefit that: the second pressure
Oil in first distributing groove 4 is beneficially transported in the second distributing groove 5 by being provided with of power pump 10.
Above-described is only some embodiments of the present invention.For the person of ordinary skill of the art, not
On the premise of departing from the invention design, it is also possible to making some deformation and improvement, these broadly fall into the protection model of the present invention
Enclose.
Claims (5)
1. coal tar product deployment device, it is characterised in that include tar distillation device (1), Colophonium chiller (2), heavy
Oil groove (3), the first distributing groove (4), the second distributing groove (5), vertical lower resistance cooling system (7), cooling back installation (8), one-tenth
Product oil groove (6) and scrubbing tower (13), described tar distillation device (1) and described Colophonium chiller (2) pass through pipeline communication,
Described Colophonium chiller (2) and described first distributing groove (4) are by pipeline communication, described heavy oil groove (3) and described first
Distributing groove (4) passes through pipeline communication, described first distributing groove (4) and described second distributing groove (5) by pipeline communication, described the
Two distributing grooves (5) and described finished product oil groove (6) are by pipeline communication, and described first distributing groove (4) top has the first flue gas and goes out
Mouth (401), described second distributing groove (5) top has the second exhanst gas outlet (501),
Described vertical lower resistance cooling system (7) includes shell body (701) and the heat exchanger tube being fixed in described shell body (701)
(703), described shell body (701) top offers passage (705), and described shell body (701) bottom is provided with condensation-water drain
(708), described shell body (701) side is provided with hot air intake (702), and described heat exchanger tube (703) is if outer wall has along longitudinal measure
Main line shape bending heat exchanging piece (704), described heat exchanger tube (703) is respectively arranged at two ends with refrigerant inlet (707) and cold-producing medium up and down
Outlet (706), described refrigerant inlet (707) and described refrigerant outlet (706) are respectively with described cooling back installation (8) even
Logical, described first exhanst gas outlet (401) and described second exhanst gas outlet (501) are respectively by pipeline and described hot air intake
(702) connection, described vertical lower resistance cooling system (7) connects with described scrubbing tower (13).
Coal tar product deployment device the most according to claim 1, it is characterised in that described heat exchanger tube (703) is hollow
Copper pipe, described wire bending heat exchanging piece (704) is the copper wire (7041) of bending, the two ends bending from beginning to end of every described copper wire (7041)
After be all welded in the outer tube wall of hollow copper tubing, and the staggered superposition of adjacent two described copper wires (7041) of each row.
Coal tar product deployment device the most according to claim 2, it is characterised in that also include multiple copper coil
(7042), described copper coil (7042) welds along the outer tube wall longitudinal direction of described heat exchanger tube (703), each copper coil (7042)
Radial direction along heat exchanger tube (703) is welded as a whole with described first copper wire (7041).
Coal tar product deployment device the most according to claim 1, it is characterised in that described heavy oil groove (3) is with described
The first compression pump (9) it is provided with between first distributing groove (4).
Coal tar product deployment device the most according to claim 1, it is characterised in that described second distributing groove (5) and institute
State and between finished product oil groove (6), be provided with the second compression pump (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610619064.9A CN106190210A (en) | 2016-08-01 | 2016-08-01 | Coal tar product deployment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610619064.9A CN106190210A (en) | 2016-08-01 | 2016-08-01 | Coal tar product deployment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106190210A true CN106190210A (en) | 2016-12-07 |
Family
ID=57498524
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610619064.9A Pending CN106190210A (en) | 2016-08-01 | 2016-08-01 | Coal tar product deployment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106190210A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3856079A (en) * | 1968-01-31 | 1974-12-24 | E Geppelt | Finned tube heat exchange conductor |
| FR2453381A1 (en) * | 1979-04-03 | 1980-10-31 | Ferodo Sa | Heat exchanger having tubes wrapped with wire - carries number of U-strips to increase surface area of tubes |
| EP0428908A1 (en) * | 1989-10-30 | 1991-05-29 | Mitsubishi Jukogyo Kabushiki Kaisha | Heat transfer pipe and method of making the same |
| CN101013013A (en) * | 2007-02-01 | 2007-08-08 | 江苏萃隆铜业有限公司 | High finned heat-exchange tube and processing method thereof |
| CN101982503A (en) * | 2010-11-12 | 2011-03-02 | 中冶焦耐(大连)工程技术有限公司 | Preparation process and device for coal tar oils |
| CN104236367A (en) * | 2013-06-06 | 2014-12-24 | 江阴新华宏铜业有限公司 | Efficient heat exchange tube |
-
2016
- 2016-08-01 CN CN201610619064.9A patent/CN106190210A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3856079A (en) * | 1968-01-31 | 1974-12-24 | E Geppelt | Finned tube heat exchange conductor |
| FR2453381A1 (en) * | 1979-04-03 | 1980-10-31 | Ferodo Sa | Heat exchanger having tubes wrapped with wire - carries number of U-strips to increase surface area of tubes |
| EP0428908A1 (en) * | 1989-10-30 | 1991-05-29 | Mitsubishi Jukogyo Kabushiki Kaisha | Heat transfer pipe and method of making the same |
| CN101013013A (en) * | 2007-02-01 | 2007-08-08 | 江苏萃隆铜业有限公司 | High finned heat-exchange tube and processing method thereof |
| CN101982503A (en) * | 2010-11-12 | 2011-03-02 | 中冶焦耐(大连)工程技术有限公司 | Preparation process and device for coal tar oils |
| CN104236367A (en) * | 2013-06-06 | 2014-12-24 | 江阴新华宏铜业有限公司 | Efficient heat exchange tube |
Non-Patent Citations (1)
| Title |
|---|
| А.Г.卡斯丘克等: "《汽轮机和燃气轮机》", 31 May 1991, 水利电力出版社 * |
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|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20161207 |