CN106110836A - A kind of cane sugar factory carbon-absorbing tower - Google Patents
A kind of cane sugar factory carbon-absorbing tower Download PDFInfo
- Publication number
- CN106110836A CN106110836A CN201610525214.XA CN201610525214A CN106110836A CN 106110836 A CN106110836 A CN 106110836A CN 201610525214 A CN201610525214 A CN 201610525214A CN 106110836 A CN106110836 A CN 106110836A
- Authority
- CN
- China
- Prior art keywords
- cleaning pipe
- pipe
- cleaning
- defogger
- tower body
- 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
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 title claims abstract description 24
- 229930006000 Sucrose Natural products 0.000 title claims abstract description 24
- 229960004793 sucrose Drugs 0.000 title claims abstract description 22
- 238000004140 cleaning Methods 0.000 claims abstract description 113
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000003546 flue gas Substances 0.000 claims abstract description 13
- 238000011049 filling Methods 0.000 claims abstract description 12
- 238000010926 purge Methods 0.000 claims abstract description 10
- 238000010521 absorption reaction Methods 0.000 claims abstract description 8
- 238000000605 extraction Methods 0.000 claims abstract description 4
- 239000007921 spray Substances 0.000 claims description 15
- 239000004744 fabric Substances 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 238000001914 filtration Methods 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 239000010865 sewage Substances 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 21
- 238000005516 engineering process Methods 0.000 description 10
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 8
- 238000007670 refining Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 235000020357 syrup Nutrition 0.000 description 5
- 239000006188 syrup Substances 0.000 description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- 240000000111 Saccharum officinarum Species 0.000 description 4
- 235000007201 Saccharum officinarum Nutrition 0.000 description 4
- 239000001569 carbon dioxide Substances 0.000 description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 description 4
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 238000005352 clarification Methods 0.000 description 2
- 238000011010 flushing procedure Methods 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 241000609240 Ambelania acida Species 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 239000010905 bagasse Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- -1 iron ion Chemical class 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 150000008442 polyphenolic compounds Chemical class 0.000 description 1
- 235000013824 polyphenols Nutrition 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000009923 sugaring Methods 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- 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
- B01D53/14—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 absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/14—Packed scrubbers
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B20/00—Purification of sugar juices
- C13B20/02—Purification of sugar juices using alkaline earth metal compounds
- C13B20/04—Purification of sugar juices using alkaline earth metal compounds followed by saturation
- C13B20/06—Purification of sugar juices using alkaline earth metal compounds followed by saturation with carbon dioxide or sulfur dioxide
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Cleaning By Liquid Or Steam (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
The invention discloses a kind of cane sugar factory carbon-absorbing tower, relate to cane sugar manufacture equipment technical field, it includes tower body, flue gas air inlet and the flue gas air outlet of boiler flue extraction discharge system it is respectively equipped with on tower body, and in tower body, it is sequentially provided with first to fourth layer from top to down, filling system it is provided with in ground floor, filling system is arranged on the top of flue gas air inlet, the spray-absorption system being interspersed it is provided with in the second layer and third layer, upper strata defogger system and lower floor's defogger system it is provided with in 4th layer, it is additionally provided with purging system in 4th layer, purging system includes cleaning pipe, lower cleaning is managed, connecting tube and drive mechanism, drive mechanism and collecting mechanism.The present invention, on the premise of ensureing that upper strata defogger system and lower floor's defogger system normally work, improves its cleaning performance and cleaning efficiency.And avoid the sewage after cleaning and dirt to spray-absorption system and the impact of filling system, improve the service life of the present invention.
Description
Technical field
The present invention relates to cane sugar manufacture equipment technical field, particularly relate to a kind of cane sugar factory carbon-absorbing tower.
Background technology
Cane sugar manufacture production technology has: sulfurous method and two kinds of techniques of carbonatation process, wherein: sulfurous method sugar refining technology due to
The more difficult removings of non-sugar impurities such as colloid in syrup, Polyphenols, iron ion, thus clarifying efficiency is lower than carbonatation process sugar refining technology.
So, the sugar product quality that sulfurous method sugar refining technology produces is poorer than the sugar product quality that carbonatation process sugar refining technology produces.
At present, sulfurous method sugar refining technology be all use Calx and sulfur dioxide as clarifier, by add ash, stove drying,
The steps such as neutralization, precipitate and separate complete the clarifying process to sugarcane juice and syrup.
Owing to sugarcane juice or syrup are being carried out using in clarifying process substantial amounts of sulfur and phosphoric acid, so the sugar product produced
Quality grade is less than carbonatation process, and sulfur content is high, and not shelf-stable, sugar loss is the biggest.Although for many years to sugarcane juice and syrup
Clarifying process is the most much studied, it is proposed that many theories and technique, but the change of its basic process is little.Recently, it was also proposed that
In carbonatation process clarification process of sugar production, direct boiler flue (low pressure low concentration) carbon dioxide makees the sugaring work of clarifier
Skill, owing to the boiler combustion instability with bagasse as fuel brings carbon dioxide in flue gas content the most on the low side but also unstable,
Giving to practice brings control extremely unstable in industrialized production, and only proposes in carbonatation process clarification process of sugar production.
Low-quality white sugar present situation and white sugar production cost residence height is produced in order to change sulfurous method sugar refining technology as early as possible
Situation under not, by the great amount of carbon dioxide recycle that contains in cane sugar factory boiler flue in sulfurous method sugar refining technology
In, Substitute For Partial sulfur, phosphoric acid also carry out full charge to sugarcane juice or syrup, use current traditional natural full charge equipment, and equipment is thrown
Entering big, utilization rate of carbon dioxide is the highest, does not reaches intended clarifying effect.
At present, when using carbon-absorbing tower to carry out Closed Circulation in Sugar Production, use to prevent demister surface dirt from affecting its function,
General by arranging purging system, when needed demister is carried out the cleaning of variable interval, but of the prior art cleaning fills
When putting with demister distant, the cleaning impulsive force cleaning device is less, it is impossible to effectively remove surface dirt, clearly
Wash weak effect, and when cleaning device and demister close together, clean device and can block the outlet of demister, affect demister
Normal work.
Summary of the invention
The present invention mainly solves the technical problem in the presence of prior art, thus provides a kind of and just ensureing demister
Often on the premise of work, the cane sugar factory carbon-absorbing tower that cleaning performance is good.
The above-mentioned technical problem of the present invention is mainly addressed by following technical proposals:
The cane sugar factory carbon-absorbing tower that the present invention provides, including tower body, described tower body is respectively equipped with boiler flue extraction
First to fourth layer it is sequentially provided with from top to down, institute in the flue gas air inlet of discharge system and flue gas air outlet, and described tower body
Being provided with filling system in stating ground floor, described filling system is arranged on the top of described flue gas air inlet, the described second layer and
It is provided with the spray-absorption system being interspersed in three layers, in described 4th layer, is provided with upper strata defogger system and demister system of lower floor
System, is additionally provided with purging system in described 4th layer, and described purging system includes cleaning pipe, lower cleaning pipe, connecting tube, driving machine
Structure and collecting mechanism；
Described upper cleaning pipe and lower cleaning pipe are arranged in parallel, and described upper cleaning is managed and described lower cleaning pipe difference position
In described upper strata defogger system and the top of lower floor's defogger system, wherein, described upper cleaning is managed and on described lower cleaning pipe
Being provided with multiple shower nozzle, the Way out of described shower nozzle is downward；
Described connecting tube is vertically arranged, and the top of described connecting tube and bottom are managed and lower cleaning pipe with described upper cleaning respectively
Being connected, its top is connected with water inlet pipe by a telescoping tube, and described telescoping tube is positioned at the inside of described tower body；
Described drive mechanism is connected with the bottom of described connecting tube, and is used for driving described connecting tube vertically
Lower movement；
Described collecting mechanism is arranged on the lower section of described lower floor defogger system, and described collecting mechanism is used for collecting described spray
The rinse water of head ejection；
And described upper cleaning pipe and lower cleaning pipe have initial bit and cleaning position, when described upper cleaning pipe and lower cleaning are managed
When being in initial bit, between spray outlet and the top of described upper strata defogger system of described upper cleaning pipe, described lower cleaning
It is provided with the first gap, when described upper cleaning is managed and lower cleaning between spray outlet and the top of described lower floor defogger system of pipe
When pipe is in cleaning position, between spray outlet and the top of described upper strata defogger system of described upper cleaning pipe, described lower clearly
Washing and be provided with the second gap between the spray outlet of pipe and the top of described lower floor defogger system, the size in described first gap is
More than 500mm, the size in described second gap is 50-100mm.
Further, described collecting mechanism includes flexible reel, filter plate, gravitation ball, driver and collecting box, described collection
Case and flexible reel are separately fixed at the left and right sides of described tower body, and described inclination of filtering plate is arranged on the inside of described tower body, and
The two ends of described filter plate are corresponding with described collecting box and flexible reel respectively, and described gravitation ball rolls and is connected to described filter plate
Upper surface, described gravitation ball is also connected with the one end collecting cloth, and the other end of described collection cloth is wrapped in described flexible reel
On, described driver is used for driving described flexible reel to rotate and regains described collection cloth.
Further, the angle of inclination of described filter plate is 30-60 °.
Further, described drive mechanism includes that Slide Box, gear and motor, described Slide Box are fixed on described tower body
On medial wall, described motor is fixed on the lateral wall of described tower body, the axle head of described motor extend into behind tower body inside with institute
Stating gear to be connected, the bottom of described connecting tube is located in described Slide Box, and the lateral wall of described connecting tube is provided with tooth
Bar, described gear and described tooth bar match.
Further, on described Slide Box, sidewall away from described tooth bar is provided with and multiple helps pulley, described in help pulley with
Match in the lateral wall of described connecting tube.
Further, the tooth bar two ends of described connecting tube further respectively have upper limit limited block and lower position block, described slip
The two ends up and down of box are additionally provided with breach, and the size of described breach is suitable with described upper limit limited block and lower position block.
Further, the described upper length cleaning pipe and lower cleaning pipe is removed with described upper strata defogger system and lower floor respectively
The length of day with fog system is corresponding.
Further, multiple described shower nozzles are average along the described upper length direction cleaning pipe and described lower cleaning pipe respectively
Distribution.
The beneficial effects of the present invention is: when upper strata defogger system and lower floor's defogger system normally work, supernatant
Wash pipe and lower cleaning pipe is in initial bit, its normal work will not be impacted, when needs are carried out, by driving machine
Structure drive connection pipe vertically moves up and down, and pipe is cleaned in drive and lower cleaning pipe moves up and down, and cleans pipe so that upper
Being switched to cleaning position with lower cleaning pipe from initial bit, the shower nozzle of upper cleaning pipe and lower cleaning pipe is to upper strata defogger system and lower floor
Defogger system carries out strong flushing, and it has been effectively ensured cleaning performance, improves cleaning efficiency.Further, by arranging collection
The rinse water of collect shower nozzle ejection, which obviates the sewage after cleaning and dirt to spray-absorption system and filling system
Impact, improves the service life of the present invention.
Accompanying drawing explanation
In order to be illustrated more clearly that the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
In having technology to describe, the required accompanying drawing used is briefly described, it should be apparent that, the accompanying drawing in describing below is only this
Some embodiments of invention, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to
Other accompanying drawing is obtained according to these accompanying drawings.
Fig. 1 is the structural representation of the cane sugar factory carbon-absorbing tower of the present invention；
Fig. 2 is the structural representation of the purging system of the cane sugar factory carbon-absorbing tower of the present invention；
Fig. 3 is the structural representation of the drive mechanism of the cane sugar factory carbon-absorbing tower of the present invention.
Detailed description of the invention
Below in conjunction with the accompanying drawings the preferred embodiments of the present invention are described in detail, so that advantages and features of the invention energy
It is easier to be readily appreciated by one skilled in the art, thus protection scope of the present invention is made apparent clear and definite defining.
Refering to shown in Fig. 1-2, the cane sugar factory carbon-absorbing tower of the present invention, including tower body 5, tower body 5 is respectively equipped with boiler smoke
First to the it is sequentially provided with from top to down in the flue gas air inlet 6 of road gas extraction discharge system and flue gas air outlet 7, and tower body 5
Four layers (1-4), is provided with filling system 12 in ground floor 1, filling system 12 is arranged on the top of flue gas air inlet 6, the second layer 2 He
It is provided with the spray-absorption system 8 being interspersed in third layer 3, in the 4th layer 4, is provided with upper strata defogger system 9 and lower floor's demister
System 10, is additionally provided with purging system 11 in the 4th layer 4, purging system 11 includes cleaning pipe 111, lower cleaning pipe 112, connecting tube
113, drive mechanism 114 and collecting mechanism 118；
Upper cleaning pipe 111 and lower cleaning pipe 112 are arranged in parallel, and upper cleaning pipe 111 and lower cleaning pipe 112 position respectively
In upper strata defogger system 9 and the top of lower floor's defogger system 10, wherein, upper cleaning pipe 111 and lower cleaning pipe 112 are provided with
Multiple shower nozzles 115, the Way out of shower nozzle 115 is downward；
Connecting tube 113 is vertically arranged, the top of connecting tube 113 and bottom respectively with upper cleaning pipe 111 and lower cleaning pipe 112
Being connected, its top is connected with water inlet pipe 117 by a telescoping tube 116, and telescoping tube 116 is positioned at the inside of tower body 5；Telescoping tube
116 are mainly used in when connecting tube 113 moves up and down, it is ensured that connecting tube 113 and the connection of water inlet pipe 117.
Drive mechanism 114 is connected with the bottom of connecting tube 113, and the most upper and lower for drive connection pipe 113
Mobile；
Collecting mechanism 118 is arranged on the lower section of lower floor's defogger system 10, and collecting mechanism 118 is used for collecting shower nozzle 115 and sprays
The rinse water gone out；
And upper cleaning pipe 111 and lower cleaning pipe 112 have initial bit and cleaning position, when upper cleaning pipe 111 and lower cleaning
When pipe 112 is in initial bit, between spray outlet and the top of upper strata defogger system 9 of upper cleaning pipe 111, lower clean pipe
It is provided with the first gap, when upper cleaning pipe 111 and lower cleaning are managed between spray outlet and the top of lower floor's defogger system 10 of 112
112 when being in cleaning position, between spray outlet and the top of upper strata defogger system 9 of upper cleaning pipe 111, lower cleaning pipe 112
Spray outlet and the top of lower floor's defogger system 10 between be provided with the second gap, the size in the first gap is more than 500mm,
The size in the second gap is 50-100mm.First gap ensure that upper strata defogger system 9 and lower floor's defogger system 10 are normal
During work, it will not be impacted by the position of upper cleaning pipe 111 and lower cleaning pipe 112, and the second gap ensure that cleaning pipe
111 and the shower nozzle of lower cleaning pipe 112 dynamics that upper strata defogger system 9 and lower floor's defogger system 10 are rinsed, quickly
Its surface dirt of cleaning.
Specifically, collecting mechanism 118 includes flexible reel 1181, filter plate 1182, gravitation ball 1183, driver 1186 and receives
Header 1185, collecting box 1185 and flexible reel 1181 are separately fixed at the left and right sides of tower body 5, and filter plate 1182 is inclined at
The inside of tower body 5, and the two ends of filter plate 1182 are corresponding with collecting box 1185 and flexible reel 1181 respectively, gravitation ball 1183 rolls
Being automatically connected in the upper surface of filter plate 1182, gravitation ball 1183 is also connected with the one end collecting cloth 1184, collects the another of cloth 1184
One ends wound is on flexible reel 1181, and driver 1184 is used for driving flexible reel 1181 to rotate and regains collection cloth 1184.?
When upper strata defogger system 9 and lower floor's defogger system 10 normally work, driver 1186 drives flexible reel 1181 to rotate and receives
Reclaiming collection cloth 1184, do not affect it and normally work, when needing the rinse water collecting shower nozzle 115 ejection, driver 1186 is motionless
Making, collection cloth 1184, under the effect of self gravitation, along the upper surface slide downward of filter plate 1182, is drawn out to by gravitation ball 1183
At collecting box 1185, the rinse water of shower nozzle 115 ejection is all introduced into collecting box 1185 after the guiding collecting cloth 1184 is collected
In, which obviate spray-absorption system 8 and the impact of filling system 12, improve the service life of the present invention.It is also preferred that the left be
Ensureing the rolling drawing effect of gravitation ball 1183, the angle of inclination of filter plate is 30-60 °.Its angle is also dependent on practical matter
Carry out reasonable set.
Refering to shown in Fig. 3, drive mechanism 114 includes Slide Box 1141, gear 1142 and motor 1143, and Slide Box 1141 is solid
Being scheduled on the medial wall of tower body 5, motor 1143 is fixed on the lateral wall of tower body 5, and the axle head of motor 1143 extend in tower body 5
Being connected with gear 1142 behind portion, the bottom of connecting tube 113 is located in Slide Box 1141, and on the lateral wall of connecting tube 113
It is provided with tooth bar 1144, gear 1142 and tooth bar 1144 to match.Driving gear 1142 to rotate by motor 1143, gear 1142 carries
Carry-over bar 1144 moves up and down, thus drive connection pipe 113, upper cleaning pipe 111 and lower cleaning pipe 112 move up and down.
It is also preferred that the left in order to ensure that connecting tube 113 will not occur catching phenomenon when moving up and down, and it is connecting tube 113
Mobile offer guide, on Slide Box 1141, sidewall away from tooth bar 1144 is provided with and multiple helps pulley 1145, helps pulley 1145
Match with the lateral wall of connecting tube 113.
In the present invention, in order to prevent the maloperation of motor 1143, tooth bar 1144 two ends of connecting tube 113 further respectively have
Limit limited block 1146 and lower position block 1147, the two ends up and down of Slide Box 1141 are additionally provided with breach 1148, the size of breach 1148
Suitable with upper limit limited block 1146 and lower position block 1147.So when connecting tube 113 moves up and down, upper limit limited block 1146
Breach 1148 can be passed with lower position block 1147, not produce with Slide Box 1141 and interfere.
In order to ensure the Integral cleaning effect of upper strata defogger system 9 and lower floor's defogger system 10, upper cleaning pipe 111 He
The length of lower cleaning pipe 112 is corresponding with the length of upper strata defogger system 9 and lower floor's defogger system 10 respectively.And, for
Making cleaning process more uniform, improve cleaning performance, multiple shower nozzles 115 are respectively along upper cleaning pipe 111 and lower cleaning pipe 112
It is evenly distributed on length direction.
In the present invention, when upper strata defogger system and lower floor's defogger system normally work, upper cleaning pipe and lower cleaning
Pipe is in initial bit, will not impact its normal work, when needs are carried out, by drive mechanism drive connection pipe
Vertically move up and down, in drive clean pipe and lower cleaning pipe move up and down so that upper clean pipe and lower cleaning pipe from
Initial bit is switched to cleaning position, and upper strata defogger system and lower floor's defogger system are entered by the shower nozzle of upper cleaning pipe and lower cleaning pipe
Row strong flushing, it has been effectively ensured cleaning performance, has improve cleaning efficiency.Further, by arranging collecting mechanism collection shower nozzle
The rinse water of ejection, which obviates the sewage after cleaning and dirt to spray-absorption system and the impact of filling system, improves
The service life of the present invention.
Above, the only detailed description of the invention of the present invention, but protection scope of the present invention is not limited thereto, any without
Cross change or replacement that creative work is expected, all should contain within protection scope of the present invention.Therefore, the protection of the present invention
Scope should be as the criterion with the protection domain that claims are limited.
Claims (8)
1. a cane sugar factory carbon-absorbing tower, including tower body, described tower body is respectively equipped with boiler flue extraction discharge system
First to fourth layer it is sequentially provided with from top to down, in described ground floor in flue gas air inlet and flue gas air outlet, and described tower body
Being provided with filling system, described filling system is arranged on the top of described flue gas air inlet, is provided with in the described second layer and third layer
The spray-absorption system being interspersed, is provided with upper strata defogger system and lower floor's defogger system, its feature in described 4th layer
Being, be additionally provided with purging system in described 4th layer, described purging system includes cleaning pipe, lower cleaning pipe, connecting tube, driving
Mechanism and collecting mechanism,
Described upper cleaning pipe and lower cleaning pipe are arranged in parallel, and described upper cleaning is managed and described lower cleaning pipe lays respectively at institute
Stating upper strata defogger system and the top of lower floor's defogger system, wherein, the described upper pipe that cleans is provided with described lower cleaning pipe
Multiple shower nozzles, the Way out of described shower nozzle is downward；
Described connecting tube is vertically arranged, and the top of described connecting tube is connected with described upper cleaning pipe and the lower pipe that cleans respectively with bottom
Logical, its top is connected with water inlet pipe by a telescoping tube, and described telescoping tube is positioned at the inside of described tower body；
Described drive mechanism is connected with the bottom of described connecting tube, and is used for driving described connecting tube to move down on vertically
Dynamic；
Described collecting mechanism is arranged on the lower section of described lower floor defogger system, and described collecting mechanism is used for collecting the spray of described shower nozzle
The rinse water gone out；
And described upper cleaning pipe and lower cleaning pipe have initial bit and cleaning position, when described upper cleaning pipe and lower cleaning pipe are in
During initial bit, between spray outlet and the top of described upper strata defogger system of described upper cleaning pipe, described lower cleaning pipe
It is provided with the first gap, when described upper cleaning is managed and at lower cleaning pipe between the top of spray outlet and described lower floor defogger system
When cleaning position, between spray outlet and the top of described upper strata defogger system of described upper cleaning pipe, described lower clean pipe
Spray outlet and the top of described lower floor defogger system between be provided with the second gap, the size in described first gap is for being more than
500mm, the size in described second gap is 50-100mm.
2. cane sugar factory carbon-absorbing tower as claimed in claim 1, it is characterised in that described collecting mechanism includes flexible reel, filter
Plate, gravitation ball, driver and collecting box, described collecting box and flexible reel are separately fixed at the left and right sides of described tower body, institute
State inclination of filtering plate and be arranged on the inside of described tower body, and the two ends of described filter plate are relative with described collecting box and flexible reel respectively
Should, described gravitation ball rolls the upper surface being connected to described filter plate, and described gravitation ball is also connected with the one end collecting cloth, described
The other end collecting cloth is wrapped on described flexible reel, and it is described that described driver is used for driving described flexible reel to rotate withdrawal
Collect cloth.
3. cane sugar factory carbon-absorbing tower as claimed in claim 2, it is characterised in that the angle of inclination of described filter plate is 30-60 °.
4. cane sugar factory carbon-absorbing tower as claimed in claim 1, it is characterised in that described drive mechanism includes Slide Box, gear
And motor, described Slide Box is fixed on the medial wall of described tower body, and described motor is fixed on the lateral wall of described tower body, institute
Stating after the axle head of motor extend into tower body inside and be connected with described gear, the bottom of described connecting tube is located in described Slide Box
In, and the lateral wall of described connecting tube is provided with tooth bar, described gear and described tooth bar and matches.
5. cane sugar factory carbon-absorbing tower as claimed in claim 4, it is characterised in that away from the side of described tooth bar on described Slide Box
Wall is provided with and multiple helps pulley, described in help pulley to match with the lateral wall of described connecting tube.
6. the cane sugar factory carbon-absorbing tower as described in claim 4 or 5, it is characterised in that the tooth bar two ends of described connecting tube are also divided
Not being provided with upper limit limited block and lower position block, the two ends up and down of described Slide Box are additionally provided with breach, the size of described breach and institute
State upper limit limited block and lower position block is suitable.
7. cane sugar factory carbon-absorbing tower as claimed in claim 6, it is characterised in that described upper cleaning is managed and the length of lower cleaning pipe
Corresponding with the length of described upper strata defogger system and lower floor's defogger system respectively.
8. cane sugar factory carbon-absorbing tower as claimed in claim 1, it is characterised in that multiple described shower nozzles are respectively along described upper cleaning
It is evenly distributed on the length direction of pipe and described lower cleaning pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610525214.XA CN106110836B (en) | 2016-07-04 | 2016-07-04 | A kind of cane sugar factory carbon-absorbing tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610525214.XA CN106110836B (en) | 2016-07-04 | 2016-07-04 | A kind of cane sugar factory carbon-absorbing tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106110836A true CN106110836A (en) | 2016-11-16 |
| CN106110836B CN106110836B (en) | 2018-06-01 |
Family
ID=57282413
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610525214.XA Expired - Fee Related CN106110836B (en) | 2016-07-04 | 2016-07-04 | A kind of cane sugar factory carbon-absorbing tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106110836B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107051011A (en) * | 2017-05-30 | 2017-08-18 | 石家庄汉创环保科技有限公司 | A kind of gas-liquid separation device of removal VOCs mists |
| CN110124344A (en) * | 2019-05-14 | 2019-08-16 | 济宁市金泰利华化工科技有限公司 | A kind of highly effective reaction rectifying column |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB503121A (en) * | 1938-04-14 | 1939-03-31 | Bohuslav Zimmerman | Process for purifying beet sugar juice |
| GB2039295B (en) * | 1978-12-04 | 1982-12-15 | Inst Forsch Ration Zuckerind | Sugar production |
| US5759283A (en) * | 1996-05-14 | 1998-06-02 | The Western Sugar Company | Method for processing sugar beets to produce a purified beet juice product |
| CN1654682A (en) * | 2005-01-21 | 2005-08-17 | 华南理工大学 | Sugar production process using boiler flue gas as clarificant |
| CN2816048Y (en) * | 2005-04-27 | 2006-09-13 | 张吉民 | Saturation filling-up apparatus for carbonation process for refining sugar |
| CN201553743U (en) * | 2009-11-30 | 2010-08-18 | 广西大学 | A kind of tank jet flow enhanced sulfur fumigation neutralization reaction device |
| CN102728200A (en) * | 2012-06-29 | 2012-10-17 | 青岛碱业股份有限公司 | Carbon absorption tower |
| CN203174110U (en) * | 2012-12-28 | 2013-09-04 | 彭思云 | Fast and efficient reverse carbonating tank |
| CN103418225A (en) * | 2013-08-08 | 2013-12-04 | 广西大新县雷平永鑫糖业有限公司 | High-efficiency carbon-absorbing tower |
| CN104437061A (en) * | 2014-12-16 | 2015-03-25 | 广西大新县雷平永鑫糖业有限公司 | Method and equipment for activating calcium carbonate from sugar refinery |
-
2016
- 2016-07-04 CN CN201610525214.XA patent/CN106110836B/en not_active Expired - Fee Related
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB503121A (en) * | 1938-04-14 | 1939-03-31 | Bohuslav Zimmerman | Process for purifying beet sugar juice |
| GB2039295B (en) * | 1978-12-04 | 1982-12-15 | Inst Forsch Ration Zuckerind | Sugar production |
| US5759283A (en) * | 1996-05-14 | 1998-06-02 | The Western Sugar Company | Method for processing sugar beets to produce a purified beet juice product |
| CN1654682A (en) * | 2005-01-21 | 2005-08-17 | 华南理工大学 | Sugar production process using boiler flue gas as clarificant |
| CN2816048Y (en) * | 2005-04-27 | 2006-09-13 | 张吉民 | Saturation filling-up apparatus for carbonation process for refining sugar |
| CN201553743U (en) * | 2009-11-30 | 2010-08-18 | 广西大学 | A kind of tank jet flow enhanced sulfur fumigation neutralization reaction device |
| CN102728200A (en) * | 2012-06-29 | 2012-10-17 | 青岛碱业股份有限公司 | Carbon absorption tower |
| CN203174110U (en) * | 2012-12-28 | 2013-09-04 | 彭思云 | Fast and efficient reverse carbonating tank |
| CN103418225A (en) * | 2013-08-08 | 2013-12-04 | 广西大新县雷平永鑫糖业有限公司 | High-efficiency carbon-absorbing tower |
| CN104437061A (en) * | 2014-12-16 | 2015-03-25 | 广西大新县雷平永鑫糖业有限公司 | Method and equipment for activating calcium carbonate from sugar refinery |
Non-Patent Citations (3)
| Title |
|---|
| 廖锦赤: "广西糖业新设备、新技术应用概述", 《广西蔗糖》 * |
| 房晓玉等: "我国甘蔗糖厂节能减排技术发展", 《甘蔗糖业》 * |
| 覃泽林等: "广西蔗糖产业技术研究进展", 《广东农业科学》 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107051011A (en) * | 2017-05-30 | 2017-08-18 | 石家庄汉创环保科技有限公司 | A kind of gas-liquid separation device of removal VOCs mists |
| CN110124344A (en) * | 2019-05-14 | 2019-08-16 | 济宁市金泰利华化工科技有限公司 | A kind of highly effective reaction rectifying column |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106110836B (en) | 2018-06-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104874255A (en) | Demisting system with dedusting, demisting and water recovery functions | |
| KR101935110B1 (en) | Washing mechanism assembly of swash plate in settling tank for water treatment system | |
| CN106110836A (en) | A kind of cane sugar factory carbon-absorbing tower | |
| CN208911525U (en) | A kind of sewage treatment settler | |
| CN103480621B (en) | A kind of crate washer | |
| CN205611719U (en) | Hierarchical edulcoration device of hot pepper | |
| CN201064699Y (en) | Baffle plate demister | |
| CN101284206A (en) | Flue gas wet desulfurization dust removing apparatus | |
| CN222567030U (en) | Internal spraying internal inflow grid dirt remover | |
| CN205815220U (en) | A kind of fibrous recovery unit being applied to the production of high transparency paper | |
| CN206063857U (en) | The shaftless anistree rolling cage assembly of oil screen bits is received in a kind of removing oil | |
| CN201581883U (en) | High-efficiency sand flushing device | |
| CN216074923U (en) | Bituminous paving maintenance all-in-one equipment | |
| CN2910986Y (en) | Rinsing machine having water tank set with runner | |
| CN201728019U (en) | Box type wet spraying fine catcher | |
| CN205760060U (en) | A kind of thick juice filter | |
| CN102380296A (en) | Desulfurizing, dust removing and purifying device | |
| CN209522857U (en) | A kind of flue gas CO2Juice thick juice saturation system | |
| CN211112664U (en) | Rope-shaped continuous washing machine | |
| CN202588249U (en) | Cascaded spiral-flow type stem washer | |
| CN221565018U (en) | Dust fall equipment for gold mine exploitation | |
| CN208440327U (en) | A kind of water-oil separating collection device | |
| CN205393060U (en) | Silk flosssilk wadding washs uses spray set | |
| CN220216254U (en) | Strip steel pretreatment device based on steel wire brush roller | |
| CN222092960U (en) | An integrated device for catalytic cracking flue gas dust removal and desulfurization |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180914 Address after: 536129 1 Yongxing Road, West Town, Hepu County, Beihai, the Guangxi Zhuang Autonomous Region. Patentee after: Guangxi Hepu west field Yongxin Sugar Industry Co.,Ltd. Address before: 532300 Lei Ping Town, Chongzuo, the Guangxi Zhuang Autonomous Region Patentee before: GUANGXI DAXIN COUNTY LEIPING YONGXIN SUGAR Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 536129 1 Yongxing Road, West Town, Hepu County, Beihai, the Guangxi Zhuang Autonomous Region. Patentee after: Guangxi Hepu Xianggui Sugar Industry Co.,Ltd. Address before: 536129 1 Yongxing Road, West Town, Hepu County, Beihai, the Guangxi Zhuang Autonomous Region. Patentee before: Guangxi Hepu west field Yongxin Sugar Industry Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180601 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |