CN207943887U - A kind of reducing type carbonators - Google Patents
A kind of reducing type carbonators Download PDFInfo
- Publication number
- CN207943887U CN207943887U CN201820184123.9U CN201820184123U CN207943887U CN 207943887 U CN207943887 U CN 207943887U CN 201820184123 U CN201820184123 U CN 201820184123U CN 207943887 U CN207943887 U CN 207943887U
- Authority
- CN
- China
- Prior art keywords
- tower circle
- tower
- cooler bin
- section
- circle
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Links
- 239000000498 cooling water Substances 0.000 claims abstract description 33
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims abstract description 24
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims description 13
- 235000017491 Bambusa tulda Nutrition 0.000 claims description 13
- 241001330002 Bambuseae Species 0.000 claims description 13
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims description 13
- 239000011425 bamboo Substances 0.000 claims description 13
- 239000007789 gas Substances 0.000 claims description 12
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical class N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 7
- 239000002912 waste gas Substances 0.000 claims description 5
- 239000010425 asbestos Substances 0.000 claims description 3
- 229910052895 riebeckite Inorganic materials 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 9
- 238000003763 carbonization Methods 0.000 abstract description 8
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 8
- 239000007788 liquid Substances 0.000 description 7
- 238000001816 cooling Methods 0.000 description 5
- 231100000241 scar Toxicity 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 4
- 235000017557 sodium bicarbonate Nutrition 0.000 description 4
- 238000011010 flushing procedure Methods 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000037390 scarring Effects 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000012452 mother liquor Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a kind of reducing type carbonators, including pedestal, it is characterised in that:The pedestal top is provided with gas distributor, the pedestal is provided with the first air inlet and soda outlet, it is provided with cooler bin section on the upside of the pedestal, if the cooler bin section includes the cooler bin of dried layer, the cooler bin is both provided with cooling water inlet and cooling water outlet, it is arranged at intervals with the first tower circle in the middle part of the cooler bin section, it is provided with the second tower circle section on the upside of the cooler bin section, if the second tower circle section includes the second tower circle of dried layer, it is provided with third tower circle section on the upside of the second tower circle section, if the third tower circle section includes dried layer third tower circle, the second tower circle section is connect with third tower circle section and cooler bin Duan Jun by conical tower circle, it is provided with tower lid on the upside of the third tower circle section;The utility model has the advantages that safety and stability, easy to maintain, production cost is low, efficient, carbonization effect is good.
Description
Technical field
The utility model belongs to carbonators equipment technical field, more particularly to a kind of reducing type carbonators.
Background technology
Carbonators is the capital equipment used in carbonisation in soda manufacture, and effect is the ammonial brine using Sol dimension method
Or the ammonia mother liquor of Hou's process for soda production carrys out absorbing carbon dioxide, and sodium bicarbonate is made, the latter's sent for calcination is then decomposed into sodium carbonate,
The big calorimetric that carbonisation is released need to be removed out of tower, and therefore, the structure of tower must satisfy the processes such as absorption, crystallization, cooling
Requirement, in alkali producing process, be carbonized inner wall of tower, and especially cooling pipe surface can form sodium bicarbonate scar layer, the activity duration gets over
Long, scar layer is thicker, and after scar layer knot is to certain thickness, since heat transfer efficiency declines and air-liquid channel becomes smaller, operation is just not
It can be normally carried out, so after carbonators general job tens hours, be cleaned, the finished product grain of the carbonators used now
Uneven, poor quality is spent, unstable quality, processing time is longer, and be carbonized inefficiency, and cooling effect is bad, carbon dioxide row
Excessive concentration is put, entreprise cost is increased.
Utility model content
The utility model is designed to provide a kind of reducing type carbonators, have safety and stability, it is easy to maintain, be produced into
This advantage low, efficient, that carbonization effect is good.
To achieve the above object, the utility model provides the following technical solutions:A kind of reducing type carbonators, including pedestal,
The pedestal top is provided with gas distributor, and the pedestal is provided with the first air inlet and soda outlet, the pedestal upside
Be provided with cooler bin section, if the cooler bin section includes the cooler bin of dried layer, the cooler bin be both provided with cooling water inlet and
Cooling water outlet, adjacent cooler bin cooling water inlet circulating water pipe is connected with cooling water outlet, set inside the cooler bin
It is equipped with cooling water pipe, the first tower circle is arranged at intervals in the middle part of the cooler bin section, the first tower circle is provided with the second air inlet,
It is provided with the second tower circle section on the upside of the cooler bin section, if the second tower circle section includes the second tower circle of dried layer, described second
It is provided with third tower circle section on the upside of tower circle section, if the third tower circle section includes dried layer third tower circle, the third tower circle is all provided with
It is equipped with hand hole, the second tower circle section is connect with third tower circle section and cooler bin Duan Jun by conical tower circle, the conical tower circle
It is provided with third air inlet and spare air inlet, the pedestal, cooler bin, the second tower circle and conical tower circle are both provided with manhole group
Part is both provided with bamboo rain-hat component, the third in the cooler bin, the first tower circle, the second tower circle, third tower circle and conical tower circle
Tower circle section is provided with ammonia salt water inlet and neutralizes water inlet, and tower lid, the tower lid setting are provided on the upside of the third tower circle section
There are steam-gas inlet, waste gas outlet and flushing interface.
Preferably, one section of circulating water pipe that the cooler bin on the upside of the first tower circle connects is provided with spare cooling water and goes out
Mouthful.
Preferably, the cooler bin is connected into circulating water pipe.
Preferably, the manhole component include manhole, the manhole cover that is set on the outside of manhole, the manhole cover is logical with manhole
It crosses and is bolted, asbestos pad is provided between manhole cover and the joint face of manhole.
Preferably, the number of plies of the cooler bin is no less than 4 layers, and the quantity for the cooling water pipe being arranged in every layer of cooler bin is many
In 10.
Preferably, the quantity of the second tower circle is at least 3.
Preferably, the bamboo rain-hat component includes sieve plate and bamboo rain-hat.
Preferably, the quantity of the conical tower circle is 2, and third air inlet and spare air inlet are separately positioned on 2 cones
Shape tower circle.
Preferably, the first tower circle is identical with the diameter of third tower circle, and less than the diameter of the second tower circle.
Compared with prior art, the beneficial effects of the utility model are as follows:
The utility model greatly facilitates the installation of carbonators, transport by multi-segment structure, effectively reduces cost, carries
The high autgmentability of tower body, increases the number of plies of the second tower circle and third tower circle, can increase high temperature section, be conducive to crystalline particle
It uniformly generates, by manhole component, convenient to overhaul and maintenance quickly cleans sodium bicarbonate scar layer, by gas distributor, uniformly
It is distributed air-flow, by the structure of bamboo rain-hat component, makes the more uniform, efficient of gas-liquid contact, reaches good gas-liquid contact effect,
It is abundant to ensure that gas-liquid exchanges, so that carbonization efficiency is significantly improved, extends contact time, product quality is high, consistency stability is good, soon
Speed reaches production requirement, reduces production cost and passes through the connection recirculated water between cooler bin by multiple cooler bin effective temperature-reducings
It manages, multiple cooling water pipes is evenly arranged in cooler bin, improve efficiency, ensure the stabilization of the temperature of cooler bin section, by multiple
The setting of spare mouth improves the adaptability of carbonators and production is effectively ensured, and reduces loss, by being arranged be relatively large in diameter second
Tower circle increases grain size number, reduces scarring speed, is conducive to working continuously for carbonators, improves yield;The utility model has
Safety and stability, the advantage that easy to maintain, production cost is low, efficient, carbonization effect is good.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is the schematic top plan view of the utility model.
In figure:1, pedestal, 2, gas distributor, the 3, first air inlet, 4, soda outlet, 5, manhole component, 6, cooler bin,
7, cooling water pipe, 8, cooling water inlet, 9, cooling water outlet, 10, circulating water pipe, 11, spare cooling water outlet, the 12, first tower
Circle, the 13, second air inlet, the 14, second tower circle, 15, conical tower circle, 16, third air inlet, 17, spare air inlet, 18, bamboo rain-hat
Component, 19, third tower circle, 20, hand hole, 21, ammonia salt water inlet, 22, neutralize water inlet, 23, steam-gas inlet, 24, waste gas outlet,
25, flushing interface, 26, Ta Gai.
Specific implementation mode
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
The every other embodiment obtained, shall fall within the protection scope of the present invention.
It please refers to Fig.1 and Fig. 2, the present embodiment provides a kind of reducing type carbonators, including pedestal 1,1 top of the pedestal is set
It is equipped with gas distributor 2, the pedestal 1 is provided with the first air inlet 3 and soda outlet 4, and 1 upside of the pedestal is provided with cooling
Case section, if the cooler bin section includes the cooler bin 6 of dried layer, the cooler bin 6 is both provided with cooling water inlet 8 and cooling water goes out
Mouth 9, the cooling water inlet 8 of adjacent cooler bin 6 and cooling water outlet 9 connect circulating water pipe 10,6 inside setting of the cooler bin
There is cooling water pipe 7, is arranged at intervals with the first tower circle 12 in the middle part of the cooler bin section, the first tower circle 12 is provided with the second air inlet
Mouth 13, the cooler bin section upside is provided with the second tower circle section, if the second tower circle section includes the second tower circle 14 of dried layer, institute
It states and is provided with third tower circle section on the upside of the second tower circle section, if the third tower circle section includes dried layer third tower circle 19, the third
Tower circle 19 is both provided with hand hole 20, and the second tower circle section is connected with third tower circle section and cooler bin Duan Jun by conical tower circle 15
It connects, the conical tower circle 15 is provided with third air inlet 16 and spare air inlet 17, the pedestal 1, cooler bin 6, the second tower circle
14 and conical tower circle 15 be both provided with manhole component 5, the cooler bin 6, the first tower circle 12, the second tower circle 14, third tower circle 19
Be both provided with bamboo rain-hat component 18 in conical tower circle 15, the third tower circle section is provided with ammonia salt water inlet 21 and neutralizes water inlet
22, the third tower circle section upside is provided with tower lid 26, and the tower lid 26 is provided with steam-gas inlet 23, waste gas outlet 24 and rinses
Interface 25.
Wherein, one section of circulating water pipe 10 that the cooler bin 6 of 12 upside of the first tower circle connects is provided with spare cooling water
Outlet 11;The cooler bin 6 is connected into circulating water pipe 10;The manhole component 5 includes manhole, the people being set on the outside of manhole
Port lid, the manhole cover are bolted with manhole, and asbestos pad is provided between manhole cover and the joint face of manhole;It is described cold
But the number of plies of case 6 is no less than 4 layers, and the quantity for the cooling water pipe 7 being arranged in every layer of cooler bin 6 is no less than 10;Second tower
The quantity of circle 14 is at least 3;The bamboo rain-hat component 18 includes sieve plate and bamboo rain-hat;The quantity of the conical tower circle 15 is 2, the
Three air inlets 16 and spare air inlet 17 are separately positioned on 2 conical tower circles 15;The first tower circle 12 and third tower circle 19
Diameter is identical, and less than the diameter of the second tower circle 14.
The utility model is using pedestal 1, gas distributor 2, the first air inlet 3, soda outlet 4, manhole component 5, cooling
Case 6, cooling water pipe 7, cooling water inlet 8, cooling water outlet 9, circulating water pipe 10, spare cooling water outlet 11, the first tower circle 12,
Second air inlet 13, the second tower circle 14, conical tower circle 15, third air inlet 16, spare air inlet 17, bamboo rain-hat component 18, third
Tower circle 19, ammonia salt water inlet 21, neutralizes water inlet 22, steam-gas inlet 23, waste gas outlet 24, flushing interface 25 and tower at hand hole 20
The combination of lid 26, the utility model greatly facilitated by multi-segment structure carbonators installation, transport, effectively reduce at
This, improves the autgmentability of tower body, increases the number of plies of the second tower circle 14 and third tower circle 19, can increase high temperature section, be conducive to
The uniform generation of crystalline particle, by manhole component 5, convenient to overhaul and maintenance quickly cleans sodium bicarbonate scar layer, passes through gas
Distributor 2, is uniformly distributed air-flow, by the structure of bamboo rain-hat component 18, makes the more uniform, efficient of gas-liquid contact, reaches good
Gas-liquid contact effect, it is abundant to ensure that gas-liquid exchanges, so that carbonization efficiency is significantly improved, extends contact time, product quality is high, one
Cause property stability is good, is rapidly achieved production requirement, reduces production cost and passes through cooler bin by 6 effective temperature-reducing of multiple cooler bins
Connection circulating water pipe 10 between 6 is evenly arranged with multiple cooling water pipes 7 in cooler bin 6, improves efficiency, ensures cooler bin section
The stabilization of temperature improve the adaptability of carbonators by the setting of multiple spare mouths and production be effectively ensured, reduce loss,
By the way that the second tower circle 14 being relatively large in diameter is arranged, increases grain size number, reduce scarring speed, be conducive to the continuous work of carbonators
Industry improves yield;In short, the utility model has, safety and stability, easy to maintain, production cost is low, efficient, carbonization effect is good
The advantages of.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is appreciated that can these embodiments be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaiied
Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.
Claims (9)
1. a kind of reducing type carbonators, including pedestal (1), it is characterised in that:Pedestal (1) top is provided with gas distributor
(2), the pedestal (1) is provided with the first air inlet (3) and soda outlet (4), and cooler bin is provided on the upside of the pedestal (1)
Section, if the cooler bin section includes the cooler bin (6) of dried layer, the cooler bin (6) is both provided with cooling water inlet (8) and cooling
Water out (9), the cooling water inlet (8) of adjacent cooler bin (6) and cooling water outlet (9) connection circulating water pipe (10), it is described
Cooler bin (6) is internally provided with cooling water pipe (7), is arranged at intervals with the first tower circle (12) in the middle part of the cooler bin section, and described the
One tower circle (12) is provided with the second air inlet (13), and the second tower circle section, the second tower circle are provided on the upside of the cooler bin section
If section includes the second tower circle (14) of dried layer, third tower circle section, the third tower circle section are provided on the upside of the second tower circle section
If including dried layer third tower circle (19), the third tower circle (19) is both provided with hand hole (20), the second tower circle section and third
Tower circle section and cooler bin Duan Jun are connected by conical tower circle (15), the conical tower circle (15) be provided with third air inlet (16) and
Spare air inlet (17), the pedestal (1), cooler bin (6), the second tower circle (14) and conical tower circle (15) are both provided with manhole group
Part (5), in the cooler bin (6), the first tower circle (12), the second tower circle (14), third tower circle (19) and conical tower circle (15)
It is provided with bamboo rain-hat component (18), the third tower circle section is provided with ammonia salt water inlet (21) and neutralizes water inlet (22), and described the
Tower lid (26) is provided on the upside of three tower circle sections, the tower lid (26) is provided with steam-gas inlet (23), waste gas outlet (24) and rinses
Interface (25).
2. reducing type carbonators according to claim 1, it is characterised in that:Cooler bin on the upside of the first tower circle (12)
(6) the one section of circulating water pipe (10) connected is provided with spare cooling water outlet (11).
3. reducing type carbonators according to claim 1, it is characterised in that:The cooler bin (6) is connected into recirculated water
It manages (10).
4. reducing type carbonators according to claim 1, it is characterised in that:The manhole component (5) includes manhole, setting
Manhole cover on the outside of manhole, the manhole cover are bolted with manhole, are arranged between manhole cover and the joint face of manhole
There is asbestos pad.
5. reducing type carbonators according to claim 1, it is characterised in that:The number of plies of the cooler bin (6) is no less than 4
The quantity of layer, the interior cooling water pipe (7) being arranged of every layer of cooler bin (6) is no less than 10.
6. reducing type carbonators according to claim 1, it is characterised in that:The quantity of the second tower circle (14) is at least
3.
7. reducing type carbonators according to claim 1, it is characterised in that:The bamboo rain-hat component (18) includes sieve plate and large bamboo hat with a conical crown and broad brim
Cap.
8. reducing type carbonators according to claim 1, it is characterised in that:The quantity of the conical tower circle (15) is 2,
Third air inlet (16) and spare air inlet (17) are separately positioned on 2 conical tower circles (15).
9. reducing type carbonators according to claim 1, it is characterised in that:The first tower circle (12) and third tower circle
(19) diameter is identical, and less than the diameter of the second tower circle (14).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201820184123.9U CN207943887U (en) | 2018-02-02 | 2018-02-02 | A kind of reducing type carbonators |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201820184123.9U CN207943887U (en) | 2018-02-02 | 2018-02-02 | A kind of reducing type carbonators |
Publications (1)
Publication Number | Publication Date |
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CN207943887U true CN207943887U (en) | 2018-10-09 |
Family
ID=63698929
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CN201820184123.9U Active CN207943887U (en) | 2018-02-02 | 2018-02-02 | A kind of reducing type carbonators |
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CN (1) | CN207943887U (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109775728A (en) * | 2019-03-22 | 2019-05-21 | 淮阴工学院 | The inlet duct of variable diameter carbonators |
CN109865418A (en) * | 2019-03-12 | 2019-06-11 | 淮阴工学院 | A kind of variable diameter carbonators lye anti-return outlet device |
CN110124589A (en) * | 2019-05-27 | 2019-08-16 | 贵州红星发展股份有限公司 | Gas-liquid reaction equipment, its system and the method for preparing barium carbonate using it |
CN111906085A (en) * | 2020-06-28 | 2020-11-10 | 淮阴工学院 | Method for optimizing cleaning effect of reducing carbonization tower as cleaning tower |
-
2018
- 2018-02-02 CN CN201820184123.9U patent/CN207943887U/en active Active
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109865418A (en) * | 2019-03-12 | 2019-06-11 | 淮阴工学院 | A kind of variable diameter carbonators lye anti-return outlet device |
CN109865418B (en) * | 2019-03-12 | 2021-09-17 | 淮阴工学院 | Alkali liquor backflow-preventing outlet device of variable-diameter carbonization tower |
CN109775728A (en) * | 2019-03-22 | 2019-05-21 | 淮阴工学院 | The inlet duct of variable diameter carbonators |
CN109775728B (en) * | 2019-03-22 | 2021-09-17 | 淮阴工学院 | Air inlet device of reducing carbonization tower |
CN110124589A (en) * | 2019-05-27 | 2019-08-16 | 贵州红星发展股份有限公司 | Gas-liquid reaction equipment, its system and the method for preparing barium carbonate using it |
CN111906085A (en) * | 2020-06-28 | 2020-11-10 | 淮阴工学院 | Method for optimizing cleaning effect of reducing carbonization tower as cleaning tower |
CN111906085B (en) * | 2020-06-28 | 2021-08-17 | 淮阴工学院 | Reducing carbonization tower |
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Effective date of registration: 20240726 Address after: 450000 Xia Wo Zhen Xi Jie Cun, Shangjie District, Zhengzhou City, Henan Province Patentee after: Henan Keneng New Material Co.,Ltd. Country or region after: China Address before: 450000 Xiawo Town, Shangjie District, Zhengzhou City, Henan Province Patentee before: HENAN CHEMICAL MACHINERY MANUFACTURING Co.,Ltd. Country or region before: China |