CN107934987A - One kind removes crystallization from wash type ammonia condensing cooling device - Google Patents
One kind removes crystallization from wash type ammonia condensing cooling device Download PDFInfo
- Publication number
- CN107934987A CN107934987A CN201711392594.5A CN201711392594A CN107934987A CN 107934987 A CN107934987 A CN 107934987A CN 201711392594 A CN201711392594 A CN 201711392594A CN 107934987 A CN107934987 A CN 107934987A
- Authority
- CN
- China
- Prior art keywords
- unit
- heat exchanger
- cooling device
- exchanger tube
- wash type
- 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
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims abstract description 90
- 229910021529 ammonia Inorganic materials 0.000 title claims abstract description 45
- 238000001816 cooling Methods 0.000 title claims abstract description 24
- 238000002425 crystallisation Methods 0.000 title claims abstract description 15
- 230000008025 crystallization Effects 0.000 title claims abstract description 15
- 235000011114 ammonium hydroxide Nutrition 0.000 claims abstract description 54
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims abstract description 52
- 239000007921 spray Substances 0.000 claims abstract description 25
- 239000000498 cooling water Substances 0.000 claims abstract description 16
- 125000004122 cyclic group Chemical group 0.000 claims abstract description 15
- 230000008676 import Effects 0.000 claims abstract description 4
- 238000007373 indentation Methods 0.000 claims description 12
- 230000004888 barrier function Effects 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 10
- 239000000908 ammonium hydroxide Substances 0.000 abstract description 34
- 238000009833 condensation Methods 0.000 abstract description 21
- 230000005494 condensation Effects 0.000 abstract description 21
- 150000003863 ammonium salts Chemical group 0.000 abstract description 8
- 238000011010 flushing procedure Methods 0.000 abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 3
- 238000004176 ammonification Methods 0.000 abstract description 2
- 230000008901 benefit Effects 0.000 abstract description 2
- 230000015556 catabolic process Effects 0.000 abstract description 2
- 238000009434 installation Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000005192 partition Methods 0.000 description 4
- 239000000571 coke Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 230000003416 augmentation Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- LELOWRISYMNNSU-UHFFFAOYSA-N hydrogen cyanide Chemical compound N#C LELOWRISYMNNSU-UHFFFAOYSA-N 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 239000012736 aqueous medium Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- -1 cyclic ammonia water Salt Chemical class 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000005381 potential energy Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000012797 qualification Methods 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/02—Preparation, purification or separation of ammonia
- C01C1/022—Preparation of aqueous ammonia solutions, i.e. ammonia water
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/06—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits having a single U-bend
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
A kind of remove of the invention is crystallized from wash type ammonia condensing cooling device, including several units, stand-by pump, cyclic ammonia water pipe, cooling water heat exchanging pipe between unit is interconnected, it is interconnected between the housing of unit, the unit of the import connection least significant end of stand-by pump, the outlet of stand-by pump connects the spray line of first unit in upper end by cyclic ammonia water pipe.The present invention can realize ammonia condensation ammonification water state, while be attached to the ammonium salt crystallization thing on heat exchanger tube from flushing heat exchanging pipe, removing using the ammonium hydroxide of condensation, and the ammonium hydroxide of condensation can recycle.The present apparatus have the advantages that condensation efficiency is high, ammonium hydroxide from rinse, recycle, stable operation, to be not required to shut-down (breakdown) mainteance, installation and adjustment convenient.
Description
Technical field
The present invention relates to chemical technology field, more particularly to a kind of remove to crystallize from wash type ammonia condensing cooling device.
Background technology
In coking industry, raw coke oven gas contains more gaseous impurities, and wherein ammonia level is more, while can also contain sulphur
Change the foreign gases such as hydrogen, hydrogen cyanide, in raw coke oven gas purification run process, raw coke oven gas is washed, the waste liquid after washing
In contain substantial amounts of ammonia and ammonium salt solution, after being separated by ammonia still process, ammonia steam will carry out effectively cooling condensation, obtain high
The ammonium hydroxide of purity.
The content of the invention
The object of the present invention is to provide one kind except crystallization is from wash type ammonia condensing cooling device, it is possible to achieve ammonia condensation into
Ammonium hydroxide state, while the ammonium salt crystallization thing on heat exchanger tube is attached to from flushing heat exchanging pipe, removing using the ammonium hydroxide of condensation, condensation
Ammonium hydroxide can recycle.
In order to achieve the above object, the present invention is realized using following technical scheme：
One kind removes crystallization from wash type ammonia condensing cooling device, including several units, stand-by pump, cyclic ammonia water
Pipe, the cooling water heat exchanging pipe between unit are interconnected, and are interconnected between the housing of unit, stand-by pump into
The unit of mouth connection least significant end, the outlet of stand-by pump connect the sprinkling of first unit in upper end by cyclic ammonia water pipe
Pipe.
In the unit, liquid point is both provided with from several units of second unit down
Cloth disk.
The liquid-distributing disk by four blocks of side plates and bottom distribution grid combine it is closed surround, four pieces of a height of 20mm of side plate~
200mm, bottom distribution grid are uniformly arranged several spray holes.
In the unit, baffling gear is both provided with from several units of the 3rd unit down
Plate.
The hydraulic barrier is provided with concave indentation, the circular hole passed through for heat exchanger tube, unilateral arcuate indentation.
The unit is 4, and the outer diameter of cooling water heat exchanging pipe is sequentially reduced from top to bottom, upper end first
The heat exchanger tube outer diameter of a unit is Φ 57mm, and heat exchange tube center distance is >=72mm~100mm；Second unit
Heat exchanger tube outer diameter be Φ 38mm, heat exchange tube center distance is >=48mm~90mm；Outside the heat exchanger tube of 3rd unit
Footpath size is Φ 25mm, and heat exchange tube center distance is >=44mm~70mm；The heat exchanger tube outer diameter of 4th unit is Φ
19mm, heat exchange tube center distance are >=25mm~60mm.
The spray hole of several Φ 2mm~Φ 20mm is symmetrically arranged in the downside of the spray line, and spray line is arranged on
The top of the unit of the top.
Compared with prior art, the beneficial effects of the invention are as follows：
One kind removes crystallization from wash type ammonia condensing cooling device, it is possible to achieve ammonia condensation ammonification water state, utilizes at the same time
The ammonium hydroxide of condensation removes the ammonium salt crystallization thing being attached on heat exchanger tube, the ammonium hydroxide of condensation can recycle from flushing heat exchanging pipe.
The present apparatus have condensation efficiency is high, ammonium hydroxide from rinse, recycle, stable operation, to be not required to shut-down (breakdown) mainteance, installation and adjustment convenient etc.
Advantage.
The present invention washes heat pipe using condensing ammonium hydroxide and be uniformly distributed backlash, using equipment pressure balance principle, passes through ammonium hydroxide
Submerge dissolving crystallized ammonium salt；Intermittent or continuity utilizes the dynamic pressure potential energy of equipment, and the ammonium of crystallization is rinsed by cyclic ammonia water
Salt, removes the ammonium salt crystallization being attached on heat exchanger tube, realizes and efficiently transmits thermal effect, obtains the ammonium hydroxide product of qualification.
Brief description of the drawings
Fig. 1 is that the present invention is a kind of except the schematic diagram crystallized from wash type ammonia condensing cooling device.
Fig. 2 is the schematic diagram of liquid stream distributing disc in the present invention.
Fig. 3 is the schematic diagram of hydraulic barrier in the present invention.
In figure：1- ammonia entrances；2- tube sheets；3- cooling water outlets；4- bobbin carriages；The unit of 5- upper ends first, 6- point
Journey partition plate；Second unit of 7-；The 3rd unit of 8-；The 4th unit of 9-；10- cooling water inlets；11- ammonia
Water out；12- stand-by pumps；13- cyclic ammonia waters pipe, 14- hydraulic barriers, 14-1 one side arcuate indentation, 14-2 concave indentations, 14-3
Circular hole, 15- liquid-distributing disks, 15-1 side plates, 15-2 bottoms distribution grid, 15-3 spray holes, 16- heat exchanger tubes, 17- housings, 18- sprays
Spill pipe.
Embodiment
The embodiment of the present invention is described further below in conjunction with the accompanying drawings：
See Fig. 1, one kind is except crystallization is from wash type ammonia condensing cooling device, including several units, stand-by pump 12, follows
Ring ammonia water pipe 13, the cooling water heat exchanging pipe between unit are interconnected, and are interconnected between the housing 17 of unit,
The unit of the import connection least significant end of stand-by pump 12, the outlet of stand-by pump 12 connects upper end first by cyclic ammonia water pipe 13
The spray line 18 of a unit 5.
In the unit, liquid is both provided with from several units of second unit 7 down
Distributing disc 15.
See Fig. 2, the liquid-distributing disk 15 by four pieces of side plate 15-1 and bottom distribution grid 15-2 combine it is closed surround, four
A height of 20mm~the 200mm of block side plate 15-1, bottom distribution grid 15-2 are uniformly arranged the spray hole of several Φ 1mm~Φ 20mm
15-3.The spacing range of spray hole 15-3 is 100mm~600mm.
In the unit, baffling is both provided with from several units of the 3rd unit 8 down
Baffle 14.
See Fig. 3, the hydraulic barrier 14 is provided with concave indentation 14-2, the circular hole 14-3 passed through for heat exchanger tube, one side
Arcuate indentation 14-1.Concave indentation 14-2 is provided through passage for liquid-distributing disk 15, and unilateral arcuate indentation 14-1 is used for ammonia
Pass through with the baffling of ammonia water mixture.
The unit is 4, and the outer diameter of cooling water heat exchanging pipe is sequentially reduced from top to bottom, heat exchanger tube 16
Arrangement to be connected through tube sheet 2 with the bobbin carriage 4 of 6 both sides of pass partition.The heat exchanger tube 16 of first unit 4 in upper end
Outer diameter is Φ 57mm, and 16 centre-to-centre spacing of heat exchanger tube is >=72mm~100mm；16 outside diameter of heat exchanger tube of second unit 7
Size is Φ 38mm, and 16 centre-to-centre spacing of heat exchanger tube is >=48mm~90mm；16 outer diameter of heat exchanger tube of 3rd unit 8 is
Φ 25mm, 16 centre-to-centre spacing of heat exchanger tube are >=44mm~70mm；16 outer diameter of heat exchanger tube of 4th unit 9 is Φ
19mm, 16 centre-to-centre spacing of heat exchanger tube are >=25mm~60mm.
The spray hole of several Φ 2mm~Φ 20mm is symmetrically arranged in the downside of the spray line 18, and spray line is set
At the top of the unit of the top.
The present invention includes four units, stand-by pump 12 and cyclic ammonia water pipe 13；Wherein four units include
Bobbin carriage 4, heat exchanger tube 16, pass partition 6, housing 17 and inlet and outlet adapter, heat exchanger tube 16 is arranged in housing 17, in housing 17
One end is provided with bobbin carriage 4, and one end of heat exchanger tube 16 is stretched out in bobbin carriage 4, and bobbin carriage 4 is divided to for two parts by pass partition 6, four
The bobbin carriage 4 of unit is interconnected by importing and exporting adapter, and cooling water is equipped with 4 bottom of bobbin carriage of the 4th unit 9
Entrance 10, in upper end, the upper end of the bobbin carriage 4 of first unit 5 is equipped with cooling water outlet 3.
The upper end of first unit 5 in upper end is equipped with ammonia entrance 1, and the lower end of the lowermost unit is equipped with ammonium hydroxide
Outlet 11.
The inside of the unit of upper end first 5 sets spray line 18, and the inside of second unit 7 sets liquid distribution
Disk 15, third and fourth unit (8,9) is internal to set hydraulic barrier 14 and liquid-distributing disk 15.Ammonia flows successively from top to bottom
The shell side of the unit 7 of unit 5, second of upper end first, the 3rd unit 8 and the 4th unit 9 is crossed,
Condensed ammonia becomes ammonium hydroxide from 11 discharge of ammonium hydroxide outlet；Cooling water flows successively through the 4th unit 9, from bottom to top
Inside the bobbin carriage 4 and heat exchanger tube 16 of three units, 8, second units 7 and upper ends, first unit 5, by cold
But water out 3 flows out.The present apparatus is countercurrent flow and the complex heat transfer flow of cross-flow heat exchange.
13 lower end of cyclic ammonia water pipe is connected with 17 bottom of housing of the 4th unit 9,13 upper end of cyclic ammonia water pipe with
The spray line 18 on first 5 housing of unit, 17 top in upper end connects, and cyclic ammonia water is in cyclic ammonia water pipe 13 by spare
12 pressurized delivereds are pumped, realize the spray line that the ammonia circulation of the 4th unit 9 is delivered to first unit 5 in upper end
18 spray out, and the cyclic ammonia water after sprinkling rinses 16 outer wall of heat exchanger tube of unit from top to bottom.
One kind provided by the invention removes crystallization：Steamed close to saturated ammonia
Vapour is entered by ammonia entrance 1 in the housing 17 of first unit 5 in upper end of ammonia condensing cooling device, and Uniform Flow passes through spray
The shell side heat exchanger tube of pipe 18 and the unit 5 of upper end first is spilt, spray line 18 can the intermittently or serially low circulation of spray temperature
Ammonium hydroxide, has cooling water Uniform Flow inside the heat exchanger tube 16 of first unit 5 in upper end, therefore, ammonia steam is in cyclic ammonia water
Under cooling effect with heat exchanger tube 16, the rapid condensation ammonium hydroxide in part, is converged, with cyclic ammonia water in 16 outer wall of heat exchanger tube successively
The heat exchanger tube 16 of lower floor is dripped to, from the part of appliance rinsed in the unit 5 of upper end first.Ammonium hydroxide after convergence continues downward
17 import of housing of second unit 7 is flowed to, second top of 7 housing of unit 17 sets liquid-distributing disk 15, use
In being uniformly distributed the ammonium hydroxide that flows down from the unit 5 of upper end first, the ammonium hydroxide after distribution continues drop and is set to second unit
Heat exchanger tube 16 inside standby 7 housings 17, since the cooling of the 16 internal flow cooling water of heat exchanger tube of second unit 7 is made
With the material that the unit 5 of upper end first transports coagulates for ammonia with separating beginning condensation, ammonia in the middle part of the mixture of ammonium hydroxide
Knot is slower, is attached to the ammonium salt that drop on heat exchanger tube 16 easily forms high concentration, and then produces crystallization, divides through liquid-distributing disk 15
The liquid to get off is flowed after cloth and washes away heat exchanger tube 16 in second 7 housing 17 of unit, from rinsing second unit 7
Interior part of appliance.Ammonium hydroxide and uncooled ammonia in second unit 7 collect follow-up afterflow by ammonium hydroxide outlet
To the inlet tube of the 3rd unit 8, uniformly divide again by the liquid-distributing disk 15 in the 3rd 8 housing 17 of unit
Cloth ammonium hydroxide, while under the cooling effect of heat exchanger tube 16, the further condensation of ammonia is realized, after becoming liquid due to gas condensation
Volume reduces, and hydraulic barrier 14 is set in the 3rd 8 housing 17 of unit, uncooled through the outside of heat exchanger tube 16 for improving
What the flow velocity of ammonia, augmentation of heat transfer, while hydraulic barrier 14 were provided with liquid-distributing disk 15 passes through passage --- concave indentation 14-
2nd, the arcuate indentation 14-1 for passing through circular hole 14-3 and baffling of heat exchanger tube 16, is used for realization the 3rd 8 housing 17 of unit
Interior ammonia condensation, since the baffling of hydraulic barrier 14 acts on, the 3rd unit 8 flows into for a central inlet, both sides
Outlet outflow, flows to the 9 ammonia entrance of unit of lower part the 4th, in the 4th 9 housing 17 of unit, ammonium hydroxide is in liquid
Distributing disc 15 is uniformly distributed under acting on, and from the crystal of 16 outer wall of flushing heat exchanging pipe, ammonia is under the condensation of heat exchanger tube 16
Coagulating liq, hydraulic barrier 14 strengthen ammonia flowing, improve heat-transfer effect, finally realize the condensation cooling procedure of ammonia, obtain
Qualified ammonium hydroxide product.
The cooling aqueous medium used of the present invention, enters from the cooling water inlet 10 of the 4th unit 9 in lower part
Device, countercurrently flows up, successively by 4 times journeys of the 4th 9 bobbin carriage of unit, the 4th 9 heat exchanger tube 16 of unit,
Journey, 4 times journeys of the 3rd 8 bobbin carriage of unit, the 3rd 8 heat exchanger tube the 16, the 3rd of unit on four 9 bobbin carriages 4 of unit
Journey, second 7 bobbin carriage of unit, 4 times journeys, second 7 heat exchanger tube of unit 16, second on a 8 bobbin carriage 4 of unit
Journey, upper end first 5 bobbin carriage of unit, 4 times journeys, 5 heat exchanger tube of unit, 16 and of upper end first on 7 bobbin carriage 4 of unit
Journey on 5 bobbin carriage 4 of the unit of upper end first, is discharged by cooling water outlet 3, realizes the reversed flow condensation cooling to ammonia.Meanwhile
Due to ammonia in condensation process there are the phase-state change that gas phase becomes liquid phase, volume reduces, therefore is tapered into using size
Heat exchanger tube and tube spacing, for augmentation of heat transfer lifting device performance.
To improve equipment performance, the present invention can close the ammonium hydroxide discharge of ammonium hydroxide outlet 11, the housing 17 of four units
Interior ammonia persistently condenses, and liquid level gradually rises ammonium hydroxide from bottom to top in the housing 17 of four units, adheres to crystallization
Heat exchanger tube 16 is completed to be immersed in ammonium hydroxide, dissolving except the ammonium salt that decrystallizes, realization device from rinsing, after flushed, ammonium hydroxide by
Outlet discharge.The present apparatus can utilize stand-by pump 12 by the ammonium hydroxide of the 4th unit 9 through circulation with intermittent or continuity
Ammonia water pipe 13, is delivered to progress ammonium hydroxide sprinkling in the spray line 18 of first unit 5 in upper end and rinses, strengthen from flushing except knot
Brilliant effect.
Described above is only the basic principle of the present invention, and not the present invention is imposed any restrictions, every right according to the present invention
It carries out equivalent variations modification and modifies to its shape, within the category of the art of this patent protection scheme.
Claims (7)
1. one kind is except crystallization is from wash type ammonia condensing cooling device, it is characterised in that including several units, stand-by pump,
Cyclic ammonia water pipe, the cooling water heat exchanging pipe between unit are interconnected, and are interconnected between the housing of unit, standby
With the unit of the import connection least significant end of pump, the outlet of stand-by pump connects the unit of the top by cyclic ammonia water pipe
Spray line.
2. a kind of remove according to claim 1 is crystallized from wash type ammonia condensing cooling device, it is characterised in that the list
In element device, liquid-distributing disk is both provided with from several units of second unit down.
3. a kind of remove according to claim 2 is crystallized from wash type ammonia condensing cooling device, it is characterised in that the liquid
Body distributing disc by four blocks of side plates and bottom distribution grid combine it is closed surround, four pieces of a height of 20mm~200mm of side plate, bottom distribution grid
It is uniformly arranged several spray holes.
4. a kind of remove according to claim 1 or 2 is crystallized from wash type ammonia condensing cooling device, it is characterised in that described
Unit in, be both provided with hydraulic barrier from several units of the 3rd unit down.
5. a kind of remove according to claim 4 is crystallized from wash type ammonia condensing cooling device, it is characterised in that the folding
Stream baffle plate setting has concave indentation, the circular hole passed through for heat exchanger tube, unilateral arcuate indentation.
6. a kind of remove according to claim 1 is crystallized from wash type ammonia condensing cooling device, it is characterised in that the list
Element device is 4, and the outer diameter of cooling water heat exchanging pipe is sequentially reduced from top to bottom, the heat exchange of first unit in upper end
Pipe outside diameter size is Φ 57mm, and heat exchange tube center distance is >=72mm~100mm；The heat exchanger tube outer diameter of second unit
For Φ 38mm, heat exchange tube center distance is >=48mm~90mm；The heat exchanger tube outer diameter of 3rd unit is Φ 25mm, is changed
Heat pipe centre-to-centre spacing is >=44mm~70mm；The heat exchanger tube outer diameter of 4th unit is Φ 19mm, and exchange heat tube center distance
For >=25mm~60mm.
7. a kind of remove according to claim 1 is crystallized from wash type ammonia condensing cooling device, it is characterised in that the sprinkling
The spray hole of several Φ 2mm~Φ 20mm is symmetrically arranged in the downside of pipe, and spray line is arranged on the unit of the top
Top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711392594.5A CN107934987B (en) | 2017-12-21 | 2017-12-21 | Remove crystallization from washing formula ammonia condensation cooling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711392594.5A CN107934987B (en) | 2017-12-21 | 2017-12-21 | Remove crystallization from washing formula ammonia condensation cooling device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107934987A true CN107934987A (en) | 2018-04-20 |
| CN107934987B CN107934987B (en) | 2024-05-14 |
Family
ID=61941011
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711392594.5A Active CN107934987B (en) | 2017-12-21 | 2017-12-21 | Remove crystallization from washing formula ammonia condensation cooling device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107934987B (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3108447A (en) * | 1960-12-23 | 1963-10-29 | Chicago Bridge & Iron Co | Refrigeration by direct vapor condensation |
| CN1337561A (en) * | 2000-08-08 | 2002-02-27 | 液体空气乔治洛德方法利用和研究有限公司 | Heat-exchanger of heat-exchanging block comprising multiple uniform fluid-distribution supply pipeline |
| CN1469774A (en) * | 2000-10-24 | 2004-01-21 | Carbamate condensation unit | |
| CN2873744Y (en) * | 2006-03-21 | 2007-02-28 | 任翱翔 | Device for quick preparing industrial ammonia water |
| CN104006581A (en) * | 2014-06-21 | 2014-08-27 | 吉首大学 | Novel ammonia refrigeration condenser |
| CN206146223U (en) * | 2016-07-12 | 2017-05-03 | 天津市晨辉饲料有限公司 | High -efficient calibration nitrogen appearance condensing equipment |
| CN106979535A (en) * | 2017-04-28 | 2017-07-25 | 北京拓首工业炉股份有限公司 | A kind of combined air air preheater with denitration function |
| CN207738464U (en) * | 2017-12-21 | 2018-08-17 | 中冶焦耐(大连)工程技术有限公司 | One kind removing crystallization from wash type ammonia condensing cooling device |
-
2017
- 2017-12-21 CN CN201711392594.5A patent/CN107934987B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3108447A (en) * | 1960-12-23 | 1963-10-29 | Chicago Bridge & Iron Co | Refrigeration by direct vapor condensation |
| CN1337561A (en) * | 2000-08-08 | 2002-02-27 | 液体空气乔治洛德方法利用和研究有限公司 | Heat-exchanger of heat-exchanging block comprising multiple uniform fluid-distribution supply pipeline |
| CN1469774A (en) * | 2000-10-24 | 2004-01-21 | Carbamate condensation unit | |
| CN2873744Y (en) * | 2006-03-21 | 2007-02-28 | 任翱翔 | Device for quick preparing industrial ammonia water |
| CN104006581A (en) * | 2014-06-21 | 2014-08-27 | 吉首大学 | Novel ammonia refrigeration condenser |
| CN206146223U (en) * | 2016-07-12 | 2017-05-03 | 天津市晨辉饲料有限公司 | High -efficient calibration nitrogen appearance condensing equipment |
| CN106979535A (en) * | 2017-04-28 | 2017-07-25 | 北京拓首工业炉股份有限公司 | A kind of combined air air preheater with denitration function |
| CN207738464U (en) * | 2017-12-21 | 2018-08-17 | 中冶焦耐(大连)工程技术有限公司 | One kind removing crystallization from wash type ammonia condensing cooling device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN107934987B (en) | 2024-05-14 |
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