CN108147488A - Rubber accelerator CBS waste water purifying equipment - Google Patents
Rubber accelerator CBS waste water purifying equipment Download PDFInfo
- Publication number
- CN108147488A CN108147488A CN201711473761.9A CN201711473761A CN108147488A CN 108147488 A CN108147488 A CN 108147488A CN 201711473761 A CN201711473761 A CN 201711473761A CN 108147488 A CN108147488 A CN 108147488A
- Authority
- CN
- China
- Prior art keywords
- perforated plate
- rubber accelerator
- accelerator cbs
- tube box
- heating evaporation
- 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.)
- Pending
Links
- 229920001971 elastomer Polymers 0.000 title claims abstract description 34
- 239000002351 wastewater Substances 0.000 title abstract description 8
- 239000000463 material Substances 0.000 claims abstract description 45
- 238000010438 heat treatment Methods 0.000 claims abstract description 42
- 238000001704 evaporation Methods 0.000 claims abstract description 32
- 230000008020 evaporation Effects 0.000 claims abstract description 31
- 238000012856 packing Methods 0.000 claims description 33
- 239000012530 fluid Substances 0.000 claims description 11
- 239000000945 filler Substances 0.000 claims description 7
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 229920000642 polymer Polymers 0.000 claims description 2
- 238000003466 welding Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 abstract description 23
- 238000013461 design Methods 0.000 abstract description 4
- 238000007789 sealing Methods 0.000 abstract description 3
- 230000008901 benefit Effects 0.000 abstract description 2
- 238000000746 purification Methods 0.000 abstract 2
- 230000000694 effects Effects 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- 238000010612 desalination reaction Methods 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 229920001195 polyisoprene Polymers 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000686 essence Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 125000000623 heterocyclic group Chemical group 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/043—Details
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/006—Water distributors either inside a treatment tank or directing the water to several treatment tanks; Water treatment plants incorporating these distributors, with or without chemical or biological tanks
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/08—Thin film evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
- C02F2103/36—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds
- C02F2103/38—Polymers
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention provides rubber accelerator CBS wastewater purification equipment which is formed by sequentially connecting an upper tube box, an upper tube plate, a heating evaporation chamber, a lower tube plate and a lower tube box. The top of the upper pipe box is provided with a material inlet, a first overflow trough in the upper pipe box consists of a first overflow tray and a first overflow weir which are of an integrated structure, and the first overflow tray is connected with a filling trough with a plurality of liquid holes at the bottom through a support column; the upper end of the side surface of the heating evaporation chamber is provided with a heating steam inlet, the lower end of the side surface of the heating evaporation chamber is provided with a heating steam outlet, and a second overflow groove arranged in the upper port of the heat exchange tube in the heating evaporation chamber is composed of a central rod, a connecting rod, an elastic sealing ring, a second overflow disc and a second overflow weir which are of an integrated structure; the bottom of the lower pipe box is provided with a material outlet, and the side surface is provided with a non-condensable gas outlet. The rubber accelerator CBS wastewater purification equipment provided by the invention has the advantages of reasonable structural design, uniform film distribution and high heat exchange efficiency.
Description
Technical field
The invention belongs to environmental technology field, more particularly, to a kind of rubber accelerator CBS effluent purifying device.
Background technology
Rubber accelerator CBS waste water salinity is high, COD concentration is high, with color and smell, and organic containing multiple heterocycles
Object, it is difficult to degrade, belong to high concentration hard-degraded organic waste water.Due to containing the stronger chlorine that is corrosive in rubber accelerator CBS waste water
Change sodium, so usually needing to carry out desalination pretreatment to it.Evaporation concentration method is one of common desalination preprocess method, rubber
After evaporation and concentration is handled, COD concentration significantly reduces accelerator CBS waste water, and coloration can be reduced to 0, and it is place to illustrate evaporation concentration method
Manage a kind of effective preprocess method of rubber accelerator CBS waste water.
Rubber accelerator CBS effluent purifying device is a kind of key equipment in evaporation concentration method, it is generally filled by cloth liquid
Put, heating evaporation room, the part such as vapor-liquid separation chamber form, operation principle is to be evaporated the material of concentration in heat exchanger tube from upper
And the heat medium outside lower flowing, with heat exchanger tube carries out heat exchange, so as to fulfill the evaporating concentration process of material.
There are following shortcomings for existing rubber accelerator CBS effluent purifying device：
(1) liquid distributor structure design is unreasonable, causes material to be processed that cannot be distributed evenly in every heat exchanger tube
On wall, the liquid film of formation is uneven, causes dry film or film breakage phenomenon, heat exchange efficiency relatively low；
(2) after heat medium enters heat exchanger, diffusion path is uncontrollable, and heat medium is formed with every heat transfer tube wall
Heat exchange cannot be equably carried out between treating material liquid film, seriously affects heat exchange efficiency.
Invention content
In view of this, the present invention is directed to propose a kind of rubber accelerator CBS effluent purifying device, to solve liquid distributor knot
Structure design it is unreasonable, heat transfer tube wall formed liquid film it is uneven, heat medium cannot sufficiently uniformly in heat exchanger tube array
The problem for the treatment of material liquid film that wall is formed carries out heat exchange, and heat exchange efficiency is relatively low.
In order to achieve the above objectives, the technical proposal of the invention is realized in this way：
A kind of rubber accelerator CBS effluent purifying device, including：
Upper tube box, top are equipped with material inlet, and the upper tube box is internally provided with the first overflow launder, support column and filler
Slot, first overflow launder are set on the underface of material inlet, and first overflow launder is equipped with the first seal cup and the first overflow
Weir, first downflow weir is set to the first seal cup surrounding, and the two is structure as a whole, the support column and the equal position of packing groove
In the first overflow tray bottom, the packing groove is connect by support column with the first seal cup, the packing groove and upper tube chamber interior wall
Connection, the bottom of the packing groove are equipped with multiple fluid apertures；
Upper perforated plate is connect with the upper tube box bottom；
Heating evaporation room is connect with the upper perforated plate bottom, heating evaporation room side upper end be equipped with heating steam into
Mouthful, side lower end is equipped with heating steam (vapor) outlet, and the first fixed link, the second fixed link and multiple foldings are equipped in the heating evaporation room
Flowing plate, the upper end of first fixed link and the upper end of the second fixed link are connect respectively with upper perforated plate, the multiple baffle plate by
Be arranged in parallel under, and fixed respectively by the first fixed link and the second fixed link successively, in the heating evaporation room be equipped with by
Multiple set of heat exchange tubes into heat exchanger tube array, the heat exchanger tube upper end stretches into upper perforated plate and connected with upper tube box, the heat exchanger tube
Upper port is internally provided with the second overflow launder, and second overflow launder is by center-pole, connecting rod, elastic seal ring, the second seal cup
It is formed with the second downflow weir, and second overflow launder has integral structure, the center-pole upper end is equipped with hollow, cylindrical shape
Elastic seal ring, the elastic seal ring is connected by connecting rod with center-pole, and the center-pole bottom end connects the second overflow
Disk, second seal cup are surrounded by the second downflow weir；
Lower perforated plate is connect with heating evaporation room bottom, and the heat exchanger tube lower end is stretched into lower perforated plate and connected with lower tube box
It is logical；
Lower tube box is connect with the lower perforated plate bottom, and the lower tube box bottom is equipped with material outlet, and side is equipped with fixed gas
Outlet.
Further, between the upper tube box and upper perforated plate, lower tube box and lower perforated plate it is riveting.
Further, first overflow launder is steamed with support column, support column and packing groove, packing groove and upper tube box, heating
It is welding between hair room and upper perforated plate, heating evaporation room and lower perforated plate.
Further, the height of first downflow weir is less than or equal to the radius of the first seal cup.
Further, the support column, material inlet and material outlet is are arranged concentrically.
Further, it is filled up in the packing groove by filler, the filler is high molecular polymer, metal or inorganic mineral
Structured packing.
Further, the equal size of fluid apertures of the filler trench bottom is identical, and adjacent fluid apertures is uniformly arranged in equilateral triangle.
Further, the number of the baffle plate is 3-5.
Further, the material of the elastic seal ring is rubber.
Relative to the prior art, a kind of rubber accelerator CBS effluent purifying device of the present invention has the advantage that：
A kind of rubber accelerator CBS effluent purifying device of the present invention can be high, difficult to degrade, complicated component to salinity
Rubber accelerator CBS waste water carries out desalination pretreatment.Compared to existing rubber accelerator CBS effluent purifying device, the present invention
Liquid distributor include：First overflow launder, packing groove and the second overflow launder have made rational improvement to the structure of liquid distributor,
Cloth liquid effect is preferable, and heat transfer tube wall can form one layer of uniform liquid film, increases heat exchange area, effectively improves evaporation effect,
And dry film and film breakage phenomenon can be prevented, extends the service life of heat exchanger tube；Rubber accelerator CBS effluent purifying device
The interior multiple baffle plates of setting, thus it is possible to vary heat exchanger tube shell side heats the flow direction of steam, makes heating steam and heat exchanger tube array
Inner wall formed treating material liquid film uniformly, be sufficiently carried out heat exchange, advantageous effect is apparent.
Description of the drawings
The attached drawing for forming the part of the present invention is used to provide further understanding of the present invention, schematic reality of the invention
Example and its explanation are applied for explaining the present invention, is not constituted improper limitations of the present invention.In the accompanying drawings：
Fig. 1 is a kind of structure diagram of rubber accelerator CBS effluent purifying device described in the embodiment of the present invention；
Fig. 2 is the structure diagram of the upper tube box and upper perforated plate described in the embodiment of the present invention；
Fig. 3 is the stereogram of the second overflow launder described in the embodiment of the present invention.
Reference sign：
1st, upper tube box；2nd, material inlet；3rd, the first overflow launder；4th, support column；5th, packing groove；6th, the first seal cup；7th,
One downflow weir；8th, fluid apertures；9th, upper perforated plate；10th, heating evaporation room；11st, steam inlet is heated；12nd, steam (vapor) outlet is heated；13rd,
One fixed link；14th, the second fixed link；15th, baffle plate；16th, heat exchanger tube；17th, the second overflow launder；18th, center-pole；19th, connecting rod；
20th, elastic seal ring；21st, the second seal cup；22nd, the second downflow weir；23rd, lower perforated plate；24th, lower tube box；25th, material outlet；26、
Fixed gas exports.
Specific embodiment
It should be noted that in the absence of conflict, the feature in embodiment and embodiment in the present invention can phase
Mutually combination.
In the description of the present invention, it is to be understood that term " " center ", " longitudinal direction ", " transverse direction ", " on ", " under ",
The orientation or position relationship of the instructions such as "front", "rear", "left", "right", " vertical ", " level ", " top ", " bottom ", " interior ", " outer " are
Based on orientation shown in the drawings or position relationship, it is for only for ease of the description present invention and simplifies description rather than instruction or dark
Show that signified device or element there must be specific orientation, with specific azimuth configuration and operation, therefore it is not intended that right
The limitation of the present invention.In addition, term " first ", " second " etc. are only used for description purpose, and it is not intended that instruction or hint phase
To importance or the implicit quantity for indicating indicated technical characteristic.The feature for defining " first ", " second " etc. as a result, can
To express or implicitly include one or more this feature.In the description of the present invention, unless otherwise indicated, " multiple "
It is meant that two or more.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " installation ", " phase
Even ", " connection " should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected or be integrally connected；It can
To be mechanical connection or be electrically connected；It can be directly connected, can also be indirectly connected by intermediary, Ke Yishi
Connection inside two elements.For the ordinary skill in the art, above-mentioned term can be understood by concrete condition
Concrete meaning in the present invention.
The present invention will be described in detail below with reference to the accompanying drawings and in conjunction with the embodiments.
As shown in Figure 1 to Figure 3, this rubber accelerator CBS effluent purifying device：
It is connected in sequence by upper tube box 1, upper perforated plate 9, heating evaporation room 10, lower perforated plate 23 and lower tube box 24.
Upper tube box 1, top are equipped with material inlet 2, and upper tube box 1 is internally provided with the first overflow launder 3, support column 4 and filler
Slot 5, the first overflow launder 3 are set on the underface of material inlet 2, and the first overflow launder 3 is equipped with the first seal cup 6 and the first downflow weir 7,
First downflow weir 7 is set to 6 surrounding of the first seal cup, and the two is structure as a whole, and the height of the first downflow weir 7 is less than or equal to
The radius of first seal cup 6.The material inlet 2 at treating material from 1 top of upper tube box adds in, and flows directly into the first overflow launder 3,
As material is continuously added, material is equably overflowed along 7 top edge of the first downflow weir, and the first overflow launder 3 plays slow well
Punching and the effect of uniform discharge.
Support column 4 and packing groove 5 are respectively positioned on 6 bottom of the first seal cup, and packing groove 5 passes through 4 and first seal cup 6 of support column
Connection, 6 outer diameter of the first seal cup are less than 5 outer diameter of packing groove, and packing groove 5 is welded with 1 inner wall of upper tube box, and the bottom of packing groove 5 is set
There is the fluid apertures 8 that multiple sizes are identical, and adjacent fluid apertures 8 is uniformly arranged in equilateral triangle.The structured packing tool filled in packing groove 5
Have capillarity, make material that gravity be overcome to be distributed evenly in entire packing groove 5, when build up of material to it is a certain amount of after,
Material overcomes surface tension effects to be uniformly distributed to each 16 inlet of heat exchanger tube by multiple fluid apertures 8 of 5 bottom of packing groove.
Upper perforated plate 9 is riveted with 1 bottom of upper tube box.
Heating evaporation room 10 is welded with 9 bottom of upper perforated plate, and 10 side upper end of heating evaporation room is equipped with heating steam inlet
11, side lower end is equipped with heating steam (vapor) outlet 12, and the first fixed link 13, the second fixed link 14 and 3- are equipped in heating evaporation room 10
The upper end of 5 baffle plates 15, the upper end of the first fixed link 13 and the second fixed link 14 is connect respectively with upper perforated plate 9,3-5 baffling
Plate 15 is from top to bottom arranged in parallel successively, and is fixed respectively by the first fixed link 13 and the second fixed link 14, heating evaporation room 10
It is interior equipped with 16 array of heat exchanger tube being made of multiple heat exchanger tubes 16,16 upper end of heat exchanger tube is stretched into upper perforated plate 9 and is connected with upper tube box 1
Logical, lower end is stretched into lower perforated plate 23 and is connected with lower tube box 24, and heat exchanger tube 16 passes through baffle plate 15, and baffle plate 15 plays support heat exchange
16 array of pipe and the effect for changing 16 shell side of heat exchanger tube heating steam direction.
16 upper port of heat exchanger tube is internally provided with the second overflow launder 17 (as shown in Figure 3), the second overflow launder 17 by center-pole 18,
Connecting rod 19, elastic seal ring 20, the second seal cup 21 and the second downflow weir 22 are formed, and there is the second overflow launder 17 one to tie
Structure, 18 upper end of center-pole be equipped with hollow, columnar caoutchouc elasticity sealing ring 20, elastic seal ring 20 by connecting rod 19 with
Center-pole 18 is connected, and 18 bottom end of center-pole connects the second seal cup 21, and the second seal cup 21 is surrounded by the second downflow weir 22.The
The caoutchouc elasticity sealing ring 20 of two overflow launders, 17 upper end has certain elasticity, can adjust fitting depth according to 16 internal diameter of heat exchanger tube
And contacted with 16 inner tight of heat exchanger tube, the outer diameter of the second seal cup 21 is slightly less than 16 internal diameter of heat exchanger tube, and material fills with second and overflows
Heat exchanger tube 16 is flowed into along 22 top edge of the second downflow weir after chute 17, uniform liquid film is formed on 16 inner wall of heat exchanger tube.
Lower perforated plate 23 is welded with 10 bottom of heating evaporation room and is riveted with 24 bottom of lower tube box.
24 bottom of lower tube box is equipped with material outlet 25, and side is equipped with fixed gas and exports 26, support column 4, material inlet 2 and object
Material outlet 25 is is arranged concentrically.
The course of work of the present invention：
The material inlet 2 at treating material from the top of upper tube box 1 adds in, and flows directly into the first overflow launder 3, and material fills with the
Equably overflowed along 7 top edge of the first downflow weir after one overflow launder 3 and flow into packing groove 5, when build up of material to it is a certain amount of after,
Material is uniformly distributed to each 16 inlet of heat exchanger tube by multiple fluid apertures 8 of 5 bottom of packing groove, and then flows into the second overflow launder
17, material fills with and flows into heat exchanger tube 16 along 22 top edge of the second downflow weir after the second overflow launder 17, on 16 inner wall of heat exchanger tube
Uniform liquid film is formed, liquid film flows from above to below.With the addition for the treatment of material, heating steam is simultaneously from heating evaporation room
The heating steam inlet 11 of 10 sides upper end enters the shell side of heat exchanger tube 16, and heating steam changes stream with the setting of baffle plate 15
Dynamic direction, the material liquid film sufficiently uniformly formed with 16 inner wall of heat exchanger tube carry out heat exchange, and part is heated steam and steamed from heating
The heating steam (vapor) outlet 12 of hair 10 side lower end of room escapes.Heat material outlet 25 of the material after concentration from 24 bottom of lower tube box
Outflow, fixed gas are escaped from the fixed gas outlet 26 of 24 side of lower tube box.
The present invention devises a kind of rubber accelerator CBS effluent purifying device, and liquid distributor of the invention includes：First overflows
Chute 3,5 and second overflow launder 17 of packing groove, liquid distributor is reasonable in design, and cloth liquid effect is preferable, 16 inner wall shape of heat exchanger tube
Into one layer of uniform liquid film, increase heat exchange area, heat exchange efficiency is improved, so that it is guaranteed that rubber accelerator CBS effluent purifying device
Reach ideal operational effect.
The liquid distributor of this rubber accelerator CBS effluent purifying device can prevent dry film and film breakage phenomenon simultaneously,
Extend the service life of heat exchanger tube 16.
It is noted that 17 strong applicability of the second overflow launder, and installation and replacement are convenient and efficient, it is time saving and energy saving.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all essences in the present invention
With within principle, any modification, equivalent replacement, improvement and so on should all be included in the protection scope of the present invention god.
Claims (9)
1. a kind of rubber accelerator CBS effluent purifying device, which is characterized in that including：
Upper tube box (1), top are equipped with material inlet (2), and the upper tube box (1) is internally provided with the first overflow launder (3), support column
(4) it is equipped with packing groove (5), first overflow launder (3) set on the underface of material inlet (2), first overflow launder (3)
First seal cup (6) and the first downflow weir (7), first downflow weir (7) are set to the first seal cup (6) surrounding, and the two
It is structure as a whole, the support column (4) and packing groove (5) are respectively positioned on the first seal cup (6) bottom, and the packing groove (5) passes through
Support column (4) is connect with the first seal cup (6), and the packing groove (5) connect with upper tube box (1) inner wall, the packing groove (5)
Bottom is equipped with multiple fluid apertures (8)；
Upper perforated plate (9) is connect with the upper tube box (1) bottom；
Heating evaporation room (10) is connect with the upper perforated plate (9) bottom, and heating evaporation room (10) the side upper end is equipped with heating
Steam inlet (11), side lower end are equipped with heating steam (vapor) outlet (12), the first fixed link are equipped in the heating evaporation room (10)
(13), the second fixed link (14) and multiple baffle plates (15), the upper end of first fixed link (13) and the second fixed link (14)
Upper end connect respectively with upper perforated plate (9), the multiple baffle plate (15) is from top to bottom arranged in parallel, and successively respectively by first
Fixed link (13) and the second fixed link (14) are fixed, are equipped with what is be made of multiple heat exchanger tubes (16) in the heating evaporation room (10)
Heat exchanger tube array, heat exchanger tube (16) upper end is stretched into upper perforated plate (9) and is connected with upper tube box (1), on the heat exchanger tube (16)
Port is internally provided with the second overflow launder (17), and second overflow launder (17) is by center-pole (18), connecting rod (19), elastic packing
(20), the second seal cup (21) and the second downflow weir (22) is enclosed to form, and second overflow launder (17) has integral structure, institute
Center-pole (18) upper end is stated equipped with hollow, columnar elastic seal ring (20), the elastic seal ring (20) passes through connection
Bar (19) is connected with center-pole (18), and center-pole (18) bottom end connects the second seal cup (21), second seal cup
(21) it is surrounded by the second downflow weir (22)；
Lower perforated plate (23) is connect with heating evaporation room (10) bottom, and lower perforated plate (23) is stretched into heat exchanger tube (16) lower end
And it is connected with lower tube box (24)；
Lower tube box (24) is connect with the lower perforated plate (23) bottom, and lower tube box (24) bottom is equipped with material outlet (25), side
Face is equipped with fixed gas and exports (26).
2. a kind of rubber accelerator CBS effluent purifying device according to claim 1, it is characterised in that：The upper tube box
(1) between upper perforated plate (9), lower tube box (24) and lower perforated plate (23) it is riveting.
3. a kind of rubber accelerator CBS effluent purifying device according to claim 1, it is characterised in that：Described first overflows
Chute (3) and support column (4), support column (4) and packing groove (5), packing groove (5) and upper tube box (1), heating evaporation room (10) with
It is welding between upper perforated plate (9), heating evaporation room (10) and lower perforated plate (23).
4. a kind of rubber accelerator CBS effluent purifying device according to claim 1, it is characterised in that：Described first overflows
The height for flowing weir (7) is less than or equal to the radius of the first seal cup (6).
5. a kind of rubber accelerator CBS effluent purifying device according to claim 1, it is characterised in that：The support column
(4), material inlet (2) is to be arranged concentrically with material outlet (25).
6. a kind of rubber accelerator CBS effluent purifying device according to claim 1, it is characterised in that：The packing groove
(5) it is filled up in by filler, the filler is high molecular polymer, metal or inorganic mineral structured packing.
7. a kind of rubber accelerator CBS effluent purifying device according to claim 1, it is characterised in that：The packing groove
(5) fluid apertures (8) of bottom size is identical, and adjacent fluid apertures (8) is uniformly arranged in equilateral triangle.
8. a kind of rubber accelerator CBS effluent purifying device according to claim 1, it is characterised in that：The baffle plate
(15) number is 3-5.
9. a kind of rubber accelerator CBS effluent purifying device according to claim 1, it is characterised in that：The elasticity is close
The material of seal (20) is rubber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711473761.9A CN108147488A (en) | 2017-12-29 | 2017-12-29 | Rubber accelerator CBS waste water purifying equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711473761.9A CN108147488A (en) | 2017-12-29 | 2017-12-29 | Rubber accelerator CBS waste water purifying equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108147488A true CN108147488A (en) | 2018-06-12 |
Family
ID=62463641
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711473761.9A Pending CN108147488A (en) | 2017-12-29 | 2017-12-29 | Rubber accelerator CBS waste water purifying equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108147488A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112479420A (en) * | 2020-11-06 | 2021-03-12 | 西安工程大学 | High-efficient oil-water separator based on electrostatic spinning nanofiber membrane |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201551862U (en) * | 2009-10-28 | 2010-08-18 | 中国石油化工股份有限公司 | Liquid distribution device of falling film evaporator |
| CN102410773A (en) * | 2010-09-21 | 2012-04-11 | 珠海格力节能环保制冷技术研究中心有限公司 | Liquid-distributing device for falling-film evaporator |
| CN105396311A (en) * | 2015-12-14 | 2016-03-16 | 深圳市瑞升华科技股份有限公司 | Falling film evaporator |
| CN208022728U (en) * | 2017-12-29 | 2018-10-30 | 天津梓煊浩柏科技有限公司 | Rubber accelerator CBS effluent treatment plant |
-
2017
- 2017-12-29 CN CN201711473761.9A patent/CN108147488A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201551862U (en) * | 2009-10-28 | 2010-08-18 | 中国石油化工股份有限公司 | Liquid distribution device of falling film evaporator |
| CN102410773A (en) * | 2010-09-21 | 2012-04-11 | 珠海格力节能环保制冷技术研究中心有限公司 | Liquid-distributing device for falling-film evaporator |
| CN105396311A (en) * | 2015-12-14 | 2016-03-16 | 深圳市瑞升华科技股份有限公司 | Falling film evaporator |
| CN208022728U (en) * | 2017-12-29 | 2018-10-30 | 天津梓煊浩柏科技有限公司 | Rubber accelerator CBS effluent treatment plant |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112479420A (en) * | 2020-11-06 | 2021-03-12 | 西安工程大学 | High-efficient oil-water separator based on electrostatic spinning nanofiber membrane |
| CN112479420B (en) * | 2020-11-06 | 2024-01-30 | 西安工程大学 | Efficient oil-water separation device based on electrostatic spinning nanofiber membrane |
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Application publication date: 20180612 |