CN106139858A - A kind of High-efficiency carbon-absorbing tower - Google Patents
A kind of High-efficiency carbon-absorbing tower Download PDFInfo
- Publication number
- CN106139858A CN106139858A CN201610514002.1A CN201610514002A CN106139858A CN 106139858 A CN106139858 A CN 106139858A CN 201610514002 A CN201610514002 A CN 201610514002A CN 106139858 A CN106139858 A CN 106139858A
- Authority
- CN
- China
- Prior art keywords
- cleaning pipe
- pipe
- defogger
- connecting tube
- cleaning
- 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
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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/62—Carbon oxides
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
Abstract
nullThe invention discloses a kind of High-efficiency 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 described tower body，And it is sequentially provided with first to fourth layer from top to down in described tower body，It is provided with filling system in described ground floor，Described filling system is arranged on the top of described flue gas air inlet，The spray-absorption system being interspersed it is provided with in the described second layer and third layer，It is provided with upper strata defogger system and lower floor's defogger system in described 4th layer，It is characterized in that，It is additionally provided with purging system in described 4th layer，Described purging system includes cleaning pipe、Lower cleaning is managed、Connecting tube and drive mechanism，The present invention is on the premise of ensureing that upper strata defogger system and lower floor's defogger system normally work，Improve its cleaning performance and cleaning efficiency.
Description
Technical field
The present invention relates to cane sugar manufacture equipment technical field, particularly relate to a kind of High-efficiency 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 High-efficiency carbon-absorbing tower to carry out Closed Circulation in Sugar Production, in order to prevent demister surface dirt from affecting its function
Use, typically by arranging purging system, when needed demister carried out the cleaning of variable interval, but of the prior art clearly
During cleaning device and demister distant, the cleaning impulsive force cleaning device is less, it is impossible to carry out surface dirt the most clear
Removing, cleaning performance is poor, and when cleaning device and demister close together, cleans device and can block the outlet of demister, impact
The normal work of demister.
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 High-efficiency 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 High-efficiency carbon-absorbing tower that the present invention provides, including tower body, described tower body is respectively equipped with boiler flue extraction and discharges
First to fourth layer it is sequentially provided with from top to down in the flue gas air inlet of system and flue gas air outlet, and described tower body, described
Being provided with filling system in one layer, described filling system is arranged on the top of described flue gas air inlet, the described second layer and third layer
Inside it is provided with the spray-absorption system being interspersed, in described 4th layer, is provided with upper strata defogger system and lower floor's defogger system,
Being additionally provided with purging system in described 4th layer, described purging system includes cleaning pipe, lower cleaning pipe, connecting tube and driving machine
Structure,
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；
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 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.
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 High-efficiency carbon-absorbing tower of the present invention；
Fig. 2 is the structural representation of the purging system of the High-efficiency carbon-absorbing tower of the present invention；
Fig. 3 is the structural representation of the drive mechanism of the High-efficiency 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 High-efficiency carbon-absorbing tower of the present invention, including tower body 5, tower body 5 is respectively equipped with boiler flue
First to fourth layer it is sequentially provided with from top to down in the flue gas air inlet 6 of extraction discharge system and flue gas air outlet 7, and tower body 5
(1-4), being 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 and the 3rd
It is provided with, in layer 3, the spray-absorption system 8 being interspersed, in the 4th layer 4, is provided with upper strata defogger system 9 and lower floor's defogger system
10, it 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
With drive mechanism 114,
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；
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, efficiently
Quickly clear up its surface dirt.
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.
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 (6)
1. a High-efficiency carbon-absorbing tower, including tower body, described tower body is respectively equipped with the flue gas of boiler flue extraction discharge system
It is sequentially provided with first to fourth layer from top to down in air inlet and flue gas air outlet, and described tower body, is provided with in described ground floor
Filling system, described filling system is arranged on the top of described flue gas air inlet, is provided with staggered in the described second layer and third layer
The spray-absorption system of distribution, is provided with upper strata defogger system and lower floor's defogger system in described 4th layer, it is characterised in that
Being additionally provided with purging system in described 4th layer, described purging system includes cleaning pipe, lower cleaning pipe, connecting tube and driving machine
Structure,
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；
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. High-efficiency carbon-absorbing tower as claimed in claim 1, it is characterised in that described drive mechanism includes Slide Box, gear and electricity
Machine, 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, described electricity
The axle head of machine is connected with described gear after extending into tower body inside, and 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 and matches.
3. High-efficiency carbon-absorbing tower as claimed in claim 2, it is characterised in that on described Slide Box on sidewall away from described tooth bar
Be provided with and multiple help pulley, described in help pulley to match with the lateral wall of described connecting tube.
4. High-efficiency carbon-absorbing tower as claimed in claim 2 or claim 3, it is characterised in that the tooth bar two ends of described connecting tube set the most respectively
Having 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 with described on
Limit limited block and lower position block are suitable.
5. High-efficiency carbon-absorbing tower as claimed in claim 4, it is characterised in that the described upper length difference cleaning pipe and lower cleaning pipe
Corresponding with the length of described upper strata defogger system and lower floor's defogger system.
6. High-efficiency carbon-absorbing tower as claimed in claim 1, it is characterised in that multiple described shower nozzles respectively along described upper clean pipe and
It is evenly distributed on the length direction of described lower cleaning pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610514002.1A CN106139858B (en) | 2016-07-04 | 2016-07-04 | A kind of High-efficiency carbon-absorbing tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610514002.1A CN106139858B (en) | 2016-07-04 | 2016-07-04 | A kind of High-efficiency carbon-absorbing tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106139858A true CN106139858A (en) | 2016-11-23 |
| CN106139858B CN106139858B (en) | 2018-10-16 |
Family
ID=57349613
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610514002.1A Active CN106139858B (en) | 2016-07-04 | 2016-07-04 | A kind of High-efficiency carbon-absorbing tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106139858B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109331582A (en) * | 2018-11-28 | 2019-02-15 | 扬州昌通照明器材有限公司 | A kind of heavy duty detergent cleaner convenient for safeguarding for air cleaning |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2039295B (en) * | 1978-12-04 | 1982-12-15 | Inst Forsch Ration Zuckerind | Sugar production |
| CN2816048Y (en) * | 2005-04-27 | 2006-09-13 | 张吉民 | Saturation filling-up apparatus for carbonation process for refining sugar |
| 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 CN201610514002.1A patent/CN106139858B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2039295B (en) * | 1978-12-04 | 1982-12-15 | Inst Forsch Ration Zuckerind | Sugar production |
| CN2816048Y (en) * | 2005-04-27 | 2006-09-13 | 张吉民 | Saturation filling-up apparatus for carbonation process for refining sugar |
| 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", 《广西糖业》 * |
| 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 (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109331582A (en) * | 2018-11-28 | 2019-02-15 | 扬州昌通照明器材有限公司 | A kind of heavy duty detergent cleaner convenient for safeguarding for air cleaning |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106139858B (en) | 2018-10-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201357153Y (en) | Pretreated glass washing production line | |
| CN108012438B (en) | A kind of pcb board ink cleaning process | |
| CN108786398B (en) | Flue gas desulfurization and regeneration integrated tower and renewable wet flue gas desulfurization method | |
| CN206950873U (en) | A kind of environmentally friendly coking flue gas desulfurization and dedusting scrubbing tower | |
| CN205288060U (en) | Desulfurization demister washing water collection device | |
| CN102909193A (en) | Direct washing filter ultrasonic cleaning device | |
| CN106110836A (en) | A kind of cane sugar factory carbon-absorbing tower | |
| CN106139858A (en) | A kind of High-efficiency carbon-absorbing tower | |
| CN205611719U (en) | Hierarchical edulcoration device of hot pepper | |
| KR20180078579A (en) | Washing mechanism assembly of swash plate in settling tank for water treatment system | |
| CN103480621B (en) | A kind of crate washer | |
| CN208275059U (en) | A kind of high energy scrubber of the positive persursor material of lithium electricity | |
| CN103881738A (en) | Organic material treatment system | |
| CN201064699Y (en) | Baffle plate demister | |
| CN103071379B (en) | Anti-scale system of flue gas desulfurizing tower for industrial pulverized coal fired boiler | |
| CN2838732Y (en) | Enhanced water bathing desulfurization dust cleaner | |
| CN202877178U (en) | Offset filter-type ultrasonic cleaning device | |
| CN209522857U (en) | A kind of flue gas CO2Juice thick juice saturation system | |
| CN103736682A (en) | Pass-type high-pressure water spraying cleaning machine | |
| CN203530240U (en) | Reduced pressure distillation tower | |
| CN102380296A (en) | Desulfurizing, dust removing and purifying device | |
| CN203569038U (en) | Fractionating tower for separation of oil products | |
| CN102895830A (en) | Washing device for acetylene gas | |
| CN105649557A (en) | Automatic control type slurry and sand separating device | |
| CN201670881U (en) | Drying roll cooling device for cleaning stage of galvanized steel strips |
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 | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 532300 Lei Ping Town, Chongzuo, the Guangxi Zhuang Autonomous Region Patentee after: Guangxi Daxin Xianggui Sugar Making Co., Ltd. Address before: 532300 Lei Ping Town, Chongzuo, the Guangxi Zhuang Autonomous Region Patentee before: Guangxi Daxin County Leiping Yongxin Sugar Co., Ltd. |
|
| CP01 | Change in the name or title of a patent holder |