CN104555159A - Rapid dispersing system with vertical heating pipeline - Google Patents
Rapid dispersing system with vertical heating pipeline Download PDFInfo
- Publication number
- CN104555159A CN104555159A CN201410819804.4A CN201410819804A CN104555159A CN 104555159 A CN104555159 A CN 104555159A CN 201410819804 A CN201410819804 A CN 201410819804A CN 104555159 A CN104555159 A CN 104555159A
- Authority
- CN
- China
- Prior art keywords
- tank body
- vertical
- pipeline
- water back
- pipe
- 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.)
- Granted
Links
- 238000010438 heat treatment Methods 0.000 title abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- 239000006185 dispersion Substances 0.000 claims description 15
- 239000000463 material Substances 0.000 abstract description 40
- 238000007599 discharging Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 5
- 239000007787 solid Substances 0.000 abstract description 4
- 239000002699 waste material Substances 0.000 abstract description 2
- 229920000297 Rayon Polymers 0.000 abstract 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 11
- 239000003546 flue gas Substances 0.000 description 11
- 239000011229 interlayer Substances 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000011344 liquid material Substances 0.000 description 3
- 230000001174 ascending effect Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000021715 photosynthesis, light harvesting Effects 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 230000004308 accommodation Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D88/00—Large containers
- B65D88/74—Large containers having means for heating, cooling, aerating or other conditioning of contents
- B65D88/744—Large containers having means for heating, cooling, aerating or other conditioning of contents heating or cooling through the walls or internal parts of the container, e.g. circulation of fluid inside the walls
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
The invention discloses a rapid dispersing system with a vertical heating pipeline. The rapid dispersing system comprises a heating pipeline which is arranged inside a tank body, wherein the heating pipeline comprises a horizontal pipeline parallel to a baseplate of the tank body and a vertical pipeline which is vertically arranged relative to the horizontal pipeline; an outlet of the horizontal pipeline is connected with an inlet of the vertical pipeline, and an outlet of the vertical pipeline is communicated with the exterior; the vertical pipeline comprises a central pipe and a plurality of branch pipelines which are circumferentially distributed by adopting the central pipe as the center. Heating medium discharged from the horizontal pipeline is divided into multiple shares to pass through the branch pipelines and the central pipe, viscose materials in the tank body are heated by utilizing the heating medium in the branch pipelines, not only can the energy waste caused by the direct discharging of the high-temperature heating medium be avoided, but also the viscose materials on the bottom and middle part inside the tank body can be simultaneously heated, the central part of the solid viscose material can be segmented into a plurality of blocks after being heated and liquefied, a core breaking effect can be realized, and the liquefying efficiency of the material can be improved.
Description
Technical field
The present invention relates to a kind of freight container tank body, relating in particular to a kind of rapid dispersion system with vertical water back of the freight container tank body for transporting sticky liquid material.
Background technology
In freight container handling load be some sticky liquid materials as pitch, refinery residues, sulphur time, because it is easy to become solid state at normal temperatures, therefore, when in liquid form these materials being packed into the container, destination is arrived through long-distance transportation, these materials just become solid-state or not runny state, and needing again to be heated into liquid state could draw off from freight container.Therefore, the heating arrangement of freight container tank body is for most important transportation tank car.At present, existing this type of generally arranges water back in tank base for the freight container tank body transporting sticky liquid material, and by the vertical pipe be communicated with water back, flue gas is directly discharged, the flue gas of about 300 DEG C is discharged to after in air, the degree of utilization of flue gas is very low, slattern quite a few heat, the efficiency of heating surface of tank body is very low, also can increase diesel consumption simultaneously.
For this reason, Chinese patent literature CN202429567U discloses a kind of pitch and spills tank car tank body, comprises the heating pipe be arranged in tank body, is also provided with interlayer in tank body, and interlayer is communicated with the chimney be arranged on outside tank body with the exhanst gas outlet of heating pipe respectively; Namely in this patent documentation, the flue gas in heating pipe enters in interlayer by exhanst gas outlet, carries out post bake, discharged after having heated by chimney again the pitch in tank body, and the heat that make use of flue gas effectively, reduces energy consumption.
But the pitch described in above-mentioned document spills in tank car tank body, although the flue gas that described interlayer can be discharged the exhanst gas outlet by described heating pipe utilizes again, but because the setting position of interlayer is limited, the flue gas that secondary utilizes only can heat the pitch corresponded in the tank body at described interlayer place again, the heat transmission of flue gas is slow, and degree of utilization is low; Therefore when this tank body utilizes flue gas to carry out post bake, not only heating location is limited, and secondary degree of utilization is low.
Summary of the invention
For this reason, technical matters to be solved by this invention is that the flue gas utilization rate in the tank body of prior art in heating pipe is low, and cause heat serious waste, energy resource consumption is large; And then provide one to make full use of flue gas heat, reduce the rapid dispersion system with vertical water back of energy loss.
For solving the problems of the technologies described above, a kind of rapid dispersion system with vertical water back of the present invention, it comprises the water back being located at tank interior, described water back comprises the horizontal pipe of the base plate setting being parallel to described tank body, and relative to the vertical pipeline that described horizontal pipe is vertically arranged; And the outlet of described horizontal pipe is connected with the entrance of described vertical pipeline, the outlet of described vertical pipeline and ft connection; Wherein, described vertical pipeline comprises a base pipe and some laterals carrying out circumference distribution centered by described base pipe.
Described base pipe comprises the spiral tube portion arranged near described base plate, and the VERTICAL TUBE portion be connected with described lateral.
The number of described lateral is set to even number, and described lateral is symmetrical between two about described base pipe.
Described lateral is set to four, and correspondence is arranged on the diagonal line of described tank body between two.
Described lateral is curved pipe, and described curved pipe forms arc convex to the tank skin direction of described tank body.
Multiple described lateral in the vertical direction centered by described base pipe forms pyramidal structure from top to bottom.
The projected length of single described lateral on the diagonal line of described tank body is 1/4th of described catercorner length.
Described arc convex is not more than 1/2nd of described tank inner chamber height to the distance of the base plate of described tank body.
The sectional area sum of described vertical pipeline is not more than the twice of the sectional area sum of described horizontal pipe.
The annular fin of umbrella-shaped structure is formed between the outer tube wall described vertical pipeline being also provided with some and described vertical pipeline.
Technique scheme of the present invention has the following advantages compared to existing technology:
1, in the present invention, described water back comprises the horizontal pipe of the base plate setting being parallel to described tank body, and relative to the vertical pipeline that described horizontal pipe is vertically arranged, and the outlet of described horizontal pipe is connected with the entrance of described vertical pipeline, the outlet of described vertical pipeline and ft connection, wherein, described vertical pipeline comprises a base pipe and some laterals carrying out circumference distribution centered by described base pipe, namely in the present invention, directly do not discharged by vertical pipeline as in the prior art by the heating medium of discharging in described horizontal pipe, but be divided into multiply to be discharged by described lateral and described base pipe after discharging in described horizontal pipe, described lateral is centered by described base pipe, carry out circumference distribution, the heating medium in described lateral can be utilized further can to heat the viscous and dense material in described tank body, high temperature heating medium not only can be avoided directly to discharge, cause energy dissipation, the viscous and dense material at described tank body inner bottom part and middle part can also be made to be heated simultaneously, the centre of the viscous and dense material of the solid shape post liquefaction that is heated is made to be divided into polylith, play brokenly core effect, improve the liquefaction efficiency of material.
2, in the present invention, described base pipe comprises the spiral tube portion arranged near described base plate, and the VERTICAL TUBE portion to be connected with described lateral, the resistance that described spiral tube portion makes heating medium be subject at base pipe is larger, can ensure that the thermal medium in horizontal pipe can flow to described lateral smoothly, the length of the halt of thermal medium in described base pipe can also be extended on the other hand, thus the heat making full use of thermal medium in pipeline heats the viscous and dense material in described tank body, improves heat utilization ratio.
3, in the present invention, the number of described lateral is set to even number, and described lateral is symmetrical between two about described base pipe; Be symmetrical arranged the viscous and dense material thermally equivalent that can make in described tank body, be beneficial to the liquefaction of material.
4, in the present invention, described lateral is set to four, and correspondence is arranged on the diagonal line of described tank body between two; Arranging of such four described laterals can carry out centre liquefaction to the viscous and dense material be cured in described tank body, realizes the broken core effect to viscous and dense material.
5, in the present invention, described lateral is curved pipe, and described curved pipe forms arc convex to the tank skin direction of described tank body; The arc of described lateral arranges and can extend the length of the halt of thermal medium in described lateral, thus the heat making full use of thermal medium in pipeline heats the viscous and dense material in described tank body, improves heat utilization ratio.
6, in the present invention, multiple described lateral in the vertical direction centered by described base pipe forms pyramidal structure from top to bottom; The viscous and dense material that post liquefaction near described lateral is convenient in the formation of pyramidal structure flows to the top of described tank body, so that the viscous and dense material also do not liquefied is heated near water back.
7, in the present invention, the projected length of single described lateral on the diagonal line of described tank body is 1/4th of described catercorner length; Or described arc convex is not more than 1/2nd of described tank inner chamber height to the distance of the base plate of described tank body; Or the sectional area sum of described vertical pipeline is not more than the twice of the sectional area sum of described horizontal pipe; These are arranged is all in described tank body, take too many space in order to avoid described lateral and have impact on total saturation of described tank body accommodation material.
8, in the present invention, the umbrella-shaped structure formed between described annular fin and the outer tube wall of described vertical pipeline can slow down the ascending velocity of the material of post liquefaction, enable the material of post liquefaction that the heat of inside is passed to solid material, prevent the material of post liquefaction be gathered in the top of described tank body with high temperature and make that head temperature is too high occurs that qualitative change situation occurs material itself.
Accompanying drawing explanation
In order to make content of the present invention be more likely to be clearly understood, below according to a particular embodiment of the invention and by reference to the accompanying drawings, the present invention is further detailed explanation, wherein
Fig. 1 is the birds-eye view of the water back in tank body of the present invention;
Fig. 2 is the water back schematic cross-section in tank body of the present invention;
In figure, Reference numeral is expressed as: 1-tank body; 11-horizontal pipe; 13-lateral; 14-arc convex; 2-base pipe; 21-spiral tube portion; 22-VERTICAL TUBE portion; 3-annular fin; 8-base plate.
Detailed description of the invention
Below in conjunction with accompanying drawing, the specific embodiment of the present invention is described in detail.Should be understood that, detailed description of the invention described herein, only for instruction and explanation of the present invention, is not limited to the present invention.
As illustrated in fig. 1 and 2, a kind of rapid dispersion system with vertical water back of the present embodiment, it comprises the water back being located at tank body 1 inside, described water back comprises the horizontal pipe 11 of the base plate setting being parallel to described tank body 1, and relative to the vertical pipeline that described horizontal pipe 11 is vertically arranged; And the outlet of described horizontal pipe 11 is connected with the entrance of described vertical pipeline, the outlet of described vertical pipeline and ft connection; Wherein, described vertical pipeline comprises a base pipe 2 and some laterals 13 carrying out circumference distribution centered by described base pipe 2.In the present embodiment, after discharging in described horizontal pipe 11, be divided into multiply by described lateral 13 and described base pipe 2 by the heating medium of discharging in described horizontal pipe 11, by because described lateral 13 be carry out centered by described base pipe 2 circumference distribution, like this, the heating medium in described lateral 13 can be utilized further can to heat the viscous and dense material in described tank body 1, high temperature heating medium not only can be avoided directly to discharge, cause energy dissipation, the viscous and dense material at described tank body 1 inner bottom part and middle part can also be made to be heated simultaneously, the centre of the viscous and dense material of the solid shape post liquefaction that is heated is made to be divided into polylith, play brokenly core effect, improve the liquefaction efficiency of material.
As preferred embodiment, described base pipe 2 comprises the spiral tube portion 21 arranged near described base plate, and the VERTICAL TUBE portion 22 be connected with described lateral; The resistance that described spiral tube portion 21 makes heating medium be subject in described base pipe 2 is larger, can ensure that the thermal medium in horizontal pipe 11 can flow to described lateral 13 smoothly, the length of the halt of thermal medium in described base pipe 2 can also be extended, thus the heat making full use of thermal medium in pipeline heats the viscous and dense material in described tank body 1, improves heat utilization ratio.
In the present embodiment, the number of described lateral 13 is set to even number, and described lateral 13 is symmetrical between two about described base pipe 2; Be symmetrical arranged the viscous and dense material thermally equivalent that can make in described tank body 1, be beneficial to the liquefaction of material.Particularly, preferred described lateral 13 is set to four, and correspondence is arranged on the diagonal line of described tank body 1 between two; Arranging of such four described laterals 13 can carry out centre liquefaction to the viscous and dense material be cured in described tank body 1, realize the broken core effect to viscous and dense material.
Further, in the present embodiment, described lateral 13 is curved pipe, and described curved pipe forms arc convex 14 to the tank skin direction of described tank body 1; The arc of described lateral 13 arranges and can extend the length of the halt of thermal medium in described lateral 13, thus the heat making full use of thermal medium in pipeline heats the viscous and dense material in described tank body 1, improves heat utilization ratio.
Meanwhile, as Fig. 2, in the present embodiment, multiple described lateral 13 in the vertical direction centered by described base pipe 2 forms pyramidal structure from top to bottom; The viscous and dense material that post liquefaction near described lateral 13 is convenient in the formation of pyramidal structure flows to the top of described tank body 1, so that the viscous and dense material also do not liquefied is heated near water back.
In described tank body 1, take too many space in order to avoid described lateral 13 and have impact on total saturation that described tank body 1 holds material, also preferred following embodiment in the present embodiment: the projected length of single described lateral 13 on the diagonal line of described tank body 1 is 1/4th of described catercorner length; Described arc convex 14 is not more than 1/2nd of described tank body 1 cavity heights to the distance of the base plate of described tank body 1; The sectional area sum of described vertical pipeline is not more than the twice of the sectional area sum of described horizontal pipe.
Further, the annular fin 3 of umbrella-shaped structure is formed between the outer tube wall described vertical pipeline being also provided with some and described vertical pipeline; The umbrella-shaped structure formed between described annular fin 3 and the outer tube wall of described lateral 13 and described base pipe 2 can slow down the ascending velocity of the material of post liquefaction, enable the material of post liquefaction that the heat of inside is passed to solid material, prevent the material of post liquefaction be gathered in the top of described tank body 1 with high temperature and make that head temperature is too high occurs that qualitative change situation occurs material itself.Wherein, number, the shape of described annular fin 3 can according to circumstances be arranged arbitrarily, if can and corresponding described lateral 13, described base pipe 2 outer tube wall between form umbrella-shaped structure.
Obviously, above-described embodiment is only for clearly example being described, and the restriction not to embodiment.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here exhaustive without the need to also giving all embodiments.And thus the apparent change of extending out or variation be still among the protection domain of the invention.
Claims (10)
1. one kind has the rapid dispersion system of vertical water back, it comprises is located at the inner water back of tank body (1), it is characterized in that: described water back comprises the horizontal pipe (11) that the base plate (8) that is parallel to described tank body (1) is arranged, and relative to the vertical pipeline that described horizontal pipe (11) is vertically arranged; And the outlet of described horizontal pipe (11) is connected with the entrance of described vertical pipeline, the outlet of described vertical pipeline and ft connection; Wherein, described vertical pipeline comprises a base pipe (2) and some laterals (13) carrying out circumference distribution centered by described base pipe (2).
2. a kind of rapid dispersion system with vertical water back according to claim 1, it is characterized in that: described base pipe (2) comprises the spiral tube portion (21) arranged near described base plate, and the VERTICAL TUBE portion (22) be connected with described lateral.
3. a kind of rapid dispersion system with vertical water back according to claim 1 and 2, it is characterized in that: the number of described lateral (13) is set to even number, and described lateral (13) is symmetrical between two about described base pipe (2).
4. a kind of rapid dispersion system with vertical water back according to claim 3, is characterized in that: described lateral (13) is set to four, and correspondence is arranged on the diagonal line of described tank body (1) between two.
5. a kind of rapid dispersion system with vertical water back according to claim 4, it is characterized in that: described lateral (13) is curved pipe, described curved pipe forms arc convex (14) to the tank skin direction of described tank body (1).
6. a kind of rapid dispersion system with vertical water back according to claim 5, is characterized in that: multiple described lateral (13) in the vertical direction centered by described base pipe (2) forms pyramidal structure from top to bottom.
7. a kind of rapid dispersion system with vertical water back according to claim 6, is characterized in that: the projected length of single described lateral (13) on the diagonal line of described tank body (1) is 1/4th of described catercorner length.
8. a kind of rapid dispersion system with vertical water back according to any one of claim 5-7, is characterized in that: described arc convex (14) is not more than 1/2nd of described tank body (1) cavity heights to the distance of the base plate (8) of described tank body (1).
9. a kind of rapid dispersion system with vertical water back according to any one of claim 1-8, is characterized in that: the sectional area sum of described vertical pipeline is not more than the twice of the sectional area sum of described horizontal pipe (11).
10. a kind of rapid dispersion system with vertical water back according to any one of claim 1-8, is characterized in that: the annular fin (3) forming umbrella-shaped structure between the outer tube wall described vertical pipeline being also provided with some and described vertical pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410819804.4A CN104555159B (en) | 2014-12-24 | 2014-12-24 | A kind of rapid dispersion system with vertical heating pipe |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410819804.4A CN104555159B (en) | 2014-12-24 | 2014-12-24 | A kind of rapid dispersion system with vertical heating pipe |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104555159A true CN104555159A (en) | 2015-04-29 |
| CN104555159B CN104555159B (en) | 2017-04-05 |
Family
ID=53072413
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410819804.4A Expired - Fee Related CN104555159B (en) | 2014-12-24 | 2014-12-24 | A kind of rapid dispersion system with vertical heating pipe |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104555159B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113788242A (en) * | 2021-11-17 | 2021-12-14 | 山东颐工材料科技股份有限公司 | Styrene storage tank is used in production of ABS high rubber powder |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE69103359T2 (en) * | 1990-03-09 | 1995-03-30 | Adryx Oil Group Nv | CONTAINER FOR TRANSPORTING A SOLID. |
| CN1129548C (en) * | 1997-01-21 | 2003-12-03 | 巴西石油公司 | Heating system for tanks for storing liquid products |
| CN202429567U (en) * | 2011-12-12 | 2012-09-12 | 西安达刚路面机械股份有限公司 | Tank body for asphalt sprinkling truck |
| CN202440575U (en) * | 2012-03-05 | 2012-09-19 | 蒋晓东 | Spinning box |
| CN203033232U (en) * | 2012-12-10 | 2013-07-03 | 天津兆华物流有限公司 | Container with direct-fired heating pipe |
| CN204368775U (en) * | 2014-12-24 | 2015-06-03 | 李延岭 | A kind of rapid dispersion system with vertical water back |
-
2014
- 2014-12-24 CN CN201410819804.4A patent/CN104555159B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE69103359T2 (en) * | 1990-03-09 | 1995-03-30 | Adryx Oil Group Nv | CONTAINER FOR TRANSPORTING A SOLID. |
| CN1129548C (en) * | 1997-01-21 | 2003-12-03 | 巴西石油公司 | Heating system for tanks for storing liquid products |
| CN202429567U (en) * | 2011-12-12 | 2012-09-12 | 西安达刚路面机械股份有限公司 | Tank body for asphalt sprinkling truck |
| CN202440575U (en) * | 2012-03-05 | 2012-09-19 | 蒋晓东 | Spinning box |
| CN203033232U (en) * | 2012-12-10 | 2013-07-03 | 天津兆华物流有限公司 | Container with direct-fired heating pipe |
| CN204368775U (en) * | 2014-12-24 | 2015-06-03 | 李延岭 | A kind of rapid dispersion system with vertical water back |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113788242A (en) * | 2021-11-17 | 2021-12-14 | 山东颐工材料科技股份有限公司 | Styrene storage tank is used in production of ABS high rubber powder |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104555159B (en) | 2017-04-05 |
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Granted publication date: 20170405 |