CN207755970U - Processing corn hydrolysis prepares the device of inositol process waste gas - Google Patents
Processing corn hydrolysis prepares the device of inositol process waste gas Download PDFInfo
- Publication number
- CN207755970U CN207755970U CN201721921362.XU CN201721921362U CN207755970U CN 207755970 U CN207755970 U CN 207755970U CN 201721921362 U CN201721921362 U CN 201721921362U CN 207755970 U CN207755970 U CN 207755970U
- Authority
- CN
- China
- Prior art keywords
- module
- spray column
- inositol
- level
- air
- 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.)
- Active
Links
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses the devices that a kind of processing corn hydrolysis prepares inositol process waste gas, are related to corn hydrolysis emission-control equipment field, to solve the problems, such as the odor pollution environment generated during corn hydrolysis prepares inositol.The utility model includes atomized water spray column, level-one fogged lye spray column, low-temperature plasma coupling UV photoelectric gas cracking deodorizing device and two level fogged lye spray column connected in sequence, and low-temperature plasma coupling UV photoelectric gas cracking deodorizing device includes low-temperature plasma deodorization section and UV photoelectric gas cracking deodorization section.The utility model is used to handle corn hydrolysis and prepares the foul smell generated during inositol.
Description
Technical field
The utility model is related to corn hydrolysis odor treating device fields, specifically, being related to a kind of processing corn hydrolysis
Prepare the device of inositol process waste gas.
Background technology
Inositol plays the role of fat metabolism and cholesterol, can reduce cholesterol, prevention of arterial is contributed to harden, moreover it is possible to
It is enough to help to remove liver fat, promote hair growth, therefore it is solid to be widely used in treating courage in cirrhosis, hepatitis, fatty liver, blood
The excessively high disease of alcohol.
The traditional production method of inositol is mainly pyrohydrolysis phytic acid, and this method equipment investment is big, and hydrolysising condition is harsh, and
And a large amount of pollutions are will produce, water at atmospheric pressure solution, microbion zymolysis etc. are then developed, there is different degrees of pollution and ask
Topic, the exhaust gas especially generated in hydrolytic process are larger to environmental pressure.
Utility model content
To solve the above problems, the utility model provides a kind of device for handling corn hydrolysis and preparing inositol process waste gas,
Exhaust gas can be handled, mitigate environmental pressure.
The utility model, including atomized water spray column connected in sequence, level-one fogged lye spray column, low-temperature plasma coupling
Close UV photoelectric gas cracking deodorizing device and two level fogged lye spray column：
Low-temperature plasma coupling UV photoelectric gas cracking deodorizing device include shell, be set to shell both ends air inlet and
Air outlet, air inlet and air outlet are connected to by air duct, are sequentially removed equipped with low-temperature plasma in the air duct of air inlet to air outlet
Smelly section and UV photoelectric gas cracking deodorization section；
Low-temperature plasma deodorization section include be set to air inlet air quantity be evenly distributed with module I and be set in air duct etc. from
Electron discharge disk, the high voltage package module that high pressure is provided for the power module I of discharging tray power supply and for discharging tray；
UV photoelectric gas cracking deodorization section includes the UV lamp that air quantity is evenly distributed with module II and is arranged after air quantity is evenly distributed with module II
Pipe and the power module II powered for UV lamp pipe.
Gas with foreign flavor after collection is dusted by atomized water spray column and preliminary purification, and alkali is atomized subsequently into level-one
Liquid spray column, the exhaust gas after alkali cleaning enter low-temperature plasma coupling UV photoelectric gas cracking deodorizing device, and exhaust gas first passes through low temperature
Plasma deodorization section carries out gas cracking purification, and macromolecular foul gas is decomposed, since the plasma reaction time is very short, for most
Limits reduce stench, so that foul smell is passed through UV photoelectric gas cracking deodorization section, by ultraviolet light and Ti-base catalyst, in wind
Decomposition reaction is carried out in road and oxygen atom oxidation, OH- oxidation reactions, final smell component are handled, and then carries out secondary alkali again
It washes, purifies exhaust gas to greatest extent.
Preferably, to protect circuit, power module I to be equipped with overcurrent protective device I, power module II is protected equipped with overcurrent
Protection unit II, UV lamp pipe are equipped with ballasting module.
Further, low-temperature plasma deodorization section is additionally provided with online spray irrigation module, and the online module that is sprayed passes through
Power module I controls and starts after plasma deodorization section works, and control module is equipped in power module I, can be realized
After discharging tray works, starts online spray irrigation module, air duct is rinsed.
Further, the air quantity is evenly distributed with module I and air quantity is evenly distributed with module II as shutter, can be manually or electric
Dynamic adjustment structure, can be evenly distributed with the exhaust gas entered from air inlet.
Further, the exhaust gas entrance of atomized water spray column is arranged in the lower end of atomized water spray column, atomized water spray column
Inside it is equipped with packing layer I, spray head I, packing layer II, spray head II and silk screen dehydrater, atomized water spray column successively from bottom to up
Top exit is connected to level-one fogged lye spray column bottom inlet；Level-one fogged lye spray column is equipped with fills out from bottom to up successively
The bed of material I, spray head I, packing layer II, spray head II and silk screen dehydrater, level-one fogged lye spray column top exit are connected to
Low-temperature plasma couples the air inlet of UV photoelectric gas cracking deodorizing device；Low-temperature plasma couples UV photoelectric gas and cracks deodorization
The air outlet of equipment is connected to the bottom inlet of two level fogged lye spray column, and two level fogged lye spray column is from bottom to up successively
Equipped with packing layer I, spray head I, packing layer II, spray head II and silk screen dehydrater, two level fogged lye spray column top exit
Place is equipped with air-introduced machine, the outlet of air-introduced machine to discharge duct, and then will treated exhaust gas direct emission.
Gas with foreign flavor after collection is dusted by atomized water spray column and preliminary purification；Exhaust gas warp after preliminary purification
Level-one fogged lye spray column is crossed, the even in liquid phase after atomization sprays on solid phase filler, from top to bottom in the gap of filler
It flows through, and soaks the liquid film that filler surface forms flowing, exhaust gas passes through packing layer from bottom to top under air-introduced machine effect, with liquid film
Mass transport process occurs for reverse contact, and the polluter in exhaust gas is absorbed, swept along, carried secretly into liquid phase, to reach purification
The purpose of exhaust gas, purified exhaust gas enter low-temperature plasma coupling UV photoelectric gas from tower top extraction and crack deodorizing device
In, the liquid phase for absorbing polluter is collected in bottom of tower, is recycled through spray pump, reaches the discharge of a certain concentration rear substitution.It splits
The exhaust gas of purification is solved by two level fogged lye spray column, free radical and ozone and residual organic matter in exhaust gas, on filler surface
Contact is absorbed, to greatest extent by waste gas purification.
Compared with prior art, the utility model has the beneficial effects that：The utility model can efficient process corn deep processing
Industry hydrolysis prepares the foul gas of inositol generation, and purification efficiency is high, anti impulsion load, invests and saves relatively, non-secondary pollution,
Function and protection are comprehensive, and operational safety is stablized, and operate with simply, spoilage is low, and maintenance is small, before promotion and application
Scape is wide.
Description of the drawings
FIG. 1 is a schematic structural view of the utility model；
Fig. 2 is atomized water spray column and fogged lye spray column structural schematic diagram in Fig. 1；
Fig. 3 is that low-temperature plasma couples UV photoelectric gas cracking deodorizing device structural schematic diagram in Fig. 1；
Fig. 4 is that low-temperature plasma couples UV photoelectric gas cracking deodorizing device circuit diagram in Fig. 1；
Fig. 5 is that air quantity is evenly distributed with module I in Fig. 1 and air quantity is evenly distributed with II structural schematic diagram of module；
Wherein, 10- atomized waters spray column；20- level-one fogged lye spray columns；30- low-temperature plasmas couple UV photoelectricity gas
Body cracks deodorizing device；40- two level fogged lye spray columns；50- air-introduced machines；
31- shells；32- air inlets；33- air outlets；34- low-temperature plasma deodorization sections；35-UV photoelectric gas cracks deodorization
Section；41- packing layers I；42- spray heads I；43- packing layers II；44- spray heads II；45- silk screen dehydraters；
341- air quantity is evenly distributed with module I；342- discharging tray；343- power modules I；344- high voltage package modules；345- sprays online
Drench wash module；346- overcurrent protective devices I；
351- air quantity is evenly distributed with module II；352-UV fluorescent tubes；353- power modules II；354- ballasting modules；355- overcurrents are protected
Protection unit II.
Specific implementation mode
The utility model is further explained below in conjunction with the accompanying drawings.
Processing corn hydrolysis described in the utility model prepares the device of inositol process waste gas, as shown in Figure 1, including sequentially
The atomized water spray column 10 of connection, level-one fogged lye spray column 20, low-temperature plasma coupling UV photoelectric gas cracking deodorization are set
Standby 30 and two level fogged lye spray column 40 and air-introduced machine 50：
The exhaust gas entrance of atomized water spray column 10 is arranged in the lower end of atomized water spray column 10, in atomized water spray column 10 from
Under it is supreme successively be equipped with packing layer I 41, spray head I 42, packing layer II 43, spray head II 44 and silk screen dehydrater 45, atomized water
10 top exit of spray column is connected to 20 bottom inlet of level-one fogged lye spray column；
Level-one fogged lye spray column 20 is equipped with packing layer I 41, lye spray head I 42, packing layer II successively from bottom to up
43, lye spray head II 44 and silk screen dehydrater 45,20 top exit of level-one fogged lye spray column are connected to low-temperature plasma
Couple the air inlet 32 of UV photoelectric gas cracking deodorizing device 30；
Low-temperature plasma couples UV photoelectric gas and cracks deodorizing device 30, as shown in Figures 3 and 4, including shell 31, is set to
The air inlet 32 and air outlet 33 at 31 both ends of shell, air inlet 32 are connected to air outlet 33 by air duct, air inlet 32 to outlet air
Low-temperature plasma deodorization section 34 and UV photoelectric gas cracking deodorization section 35 are sequentially equipped in the air duct of mouth 33：
Low-temperature plasma deodorization section 34 includes being set to the air quantity of air inlet 32 to be evenly distributed with module I 341 (air quantity is evenly distributed with module I
341 take adjustable venetian blind type, and structure is as shown in Figure 5) and it is set to plasma discharge disk 342 in air duct, for electric discharge
The power module I 343 of the power supply of disk 342 and the high voltage package module 344 that high pressure is provided for low-temperature plasma deodorization section 34, power supply
Overcurrent protective device I 346 is additionally provided in module I 343, low-temperature plasma deodorization section 34 further includes online spray irrigation module 345,
The online module 345 that is sprayed is controlled by power module I 343, and control module is equipped in power module I 343, can be realized
After discharging tray 342 works, starts online spray irrigation module 345, air duct is rinsed.
UV photoelectric gas cracking deodorization section 35 including air quantity is evenly distributed with module II 351, and (it is adjustable that air quantity, which is evenly distributed with module II 351,
Venetian blind type, structure is as shown in Figure 5) and be arranged after air quantity is evenly distributed with module II 351 UV lamp pipe 352, be arranged in UV lamp pipe
Ballasting module 354 on 352 and the power module II 353 for the power supply of UV lamp pipe 352, power module II 353 are protected equipped with overcurrent
Protection unit II 355.
Two level fogged lye spray column 40 is equipped with packing layer I 41, spray head I 42, packing layer II 43, spray successively from bottom to up
Head II 44 and silk screen dehydrater 45 are drenched, the air outlet 33 of low-temperature plasma coupling UV photoelectric gas cracking deodorizing device 30 is connected to
40 bottom exhaust gas entrance of two level fogged lye spray column is equipped with air-introduced machine 50 at 40 top exit of two level fogged lye spray column,
The outlet of air-introduced machine 50, and then will treated exhaust gas direct emission to discharge duct.
In the utility model, the direction of motion of exhaust gas is as shown by the arrows in Figure 1.Exhaust gas after collection, sprays by atomized water
Leaching tower 10 is dusted and preliminary purification, then passes through level-one fogged lye spray column 20, and the polluter in exhaust gas is absorbed,
Exhaust gas after double purification enters in low-temperature plasma coupling UV photoelectric gas cracking deodorizing device 30, is removed in low-temperature plasma
Smelly section 34 macromolecular foul smell is decomposed, is decomposed small molecule foul smell subsequently into UV photoelectric gas cracking deodorization section 35, cracking is net
Exhaust gas after change is by two level fogged lye spray column 40, free radical and ozone and residual organic matter in exhaust gas, on filler surface
Contact is absorbed, and will be discharged after waste gas purification to greatest extent.
Claims (8)
1. a kind of processing corn hydrolysis prepares the device of inositol process waste gas, which is characterized in that including atomized water connected in sequence
Spray column (10), level-one fogged lye spray column (20), low-temperature plasma coupling UV photoelectric gas cracking deodorizing device (30) and
Two level fogged lye spray column (40)：
Low-temperature plasma coupling UV photoelectric gas cracking deodorizing device (30) includes shell (31), is set to shell (31) both ends
Air inlet (32) and air outlet (33), air inlet (32) and air outlet (33) are connected to by air duct, air inlet (32) to air outlet
(33) low-temperature plasma deodorization section (34) and UV photoelectric gas cracking deodorization section (35) are sequentially equipped in air duct；
Low-temperature plasma deodorization section (34) is evenly distributed with module I (341) and is set to wind including being set to the air quantity of air inlet (32)
Plasma discharge disk (342) in road is the power module I (343) of discharging tray (342) power supply and is that discharging tray (342) carries
For the high voltage package module (344) of high pressure；
UV photoelectric gas cracking deodorization section (35) includes that air quantity be evenly distributed with module II (351) and setting in air quantity is evenly distributed with module II
(351) the UV lamp pipe (352) after and the power module II (353) for UV lamp pipe (352) power supply.
2. processing corn hydrolysis according to claim 1 prepares the device of inositol process waste gas, which is characterized in that power supply mould
Block I (343) is equipped with overcurrent protective device I (346), and power module II (353) is equipped with overcurrent protective device II (355), UV
Fluorescent tube (352) is equipped with ballasting module (354).
3. processing corn hydrolysis according to claim 1 prepares the device of inositol process waste gas, which is characterized in that low temperature etc.
Ion deodorization section (34) is additionally provided with online spray irrigation module (345), is sprayed module (345) online and passes through power module I
(343) it controls and starts after discharging tray (342) work.
4. processing corn hydrolysis according to claim 1 prepares the device of inositol process waste gas, which is characterized in that the wind
It is shutter that the uniformly distributed module I (341) of amount and air quantity, which are evenly distributed with module II (351),.
5. the processing corn hydrolysis according to claim 1-4 any claims prepares the device of inositol process waste gas,
It is characterized in that, atomized water spray column (10) lower end is equipped with exhaust gas entrance, is equipped with successively from bottom to up in atomized water spray column (10)
Packing layer I (41), spray head I (42), packing layer II (43), spray head II (44) and silk screen dehydrater (45) are atomized water spray
Tower (10) top exit is connected to level-one fogged lye spray column (20) bottom exhaust gas entrance.
6. processing corn hydrolysis according to claim 5 prepares the device of inositol process waste gas, which is characterized in that level-one mist
Choline liquid spray column (20) is equipped with packing layer I (41), spray head I (42), packing layer II (43), spray head II successively from bottom to up
(44) and silk screen dehydrater (45), level-one fogged lye spray column (20) top exit are connected to low-temperature plasma coupling UV photoelectricity
Gas cracks the air inlet (32) of deodorizing device (30).
7. processing corn hydrolysis according to claim 6 prepares the device of inositol process waste gas, which is characterized in that two level mist
Choline liquid spray column (40) is equipped with packing layer I (41), spray head I (42), packing layer II (43), spray head II successively from bottom to up
(44) and silk screen dehydrater (45), low-temperature plasma couple air outlet (33) connection of UV photoelectric gas cracking deodorizing device (30)
To two level fogged lye spray column (40) bottom exhaust gas entrance.
8. processing corn hydrolysis according to claim 7 prepares the device of inositol process waste gas, which is characterized in that two level mist
Air-introduced machine (50), the outlet of air-introduced machine (50) to discharge duct are equipped at choline liquid spray column (40) top exit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721921362.XU CN207755970U (en) | 2017-12-29 | 2017-12-29 | Processing corn hydrolysis prepares the device of inositol process waste gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721921362.XU CN207755970U (en) | 2017-12-29 | 2017-12-29 | Processing corn hydrolysis prepares the device of inositol process waste gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207755970U true CN207755970U (en) | 2018-08-24 |
Family
ID=63182836
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721921362.XU Active CN207755970U (en) | 2017-12-29 | 2017-12-29 | Processing corn hydrolysis prepares the device of inositol process waste gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207755970U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111450660A (en) * | 2020-04-08 | 2020-07-28 | 浙江大维高新技术股份有限公司 | Landfill leachate odor purification device and process thereof |
-
2017
- 2017-12-29 CN CN201721921362.XU patent/CN207755970U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111450660A (en) * | 2020-04-08 | 2020-07-28 | 浙江大维高新技术股份有限公司 | Landfill leachate odor purification device and process thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN208066104U (en) | A kind of chemical industry waste water station foul smell is collected and processing system | |
| CN108361723A (en) | A kind of industrial waste-gas purifier and operating method | |
| CN108310941A (en) | A kind of waste gas treatment device and method | |
| CN104275086A (en) | Wet oxidation desulfurization method and device | |
| CN208082181U (en) | A kind of waste gas treatment device | |
| CN110314507A (en) | It is a kind of to print organic waste gas treatment process and processing system | |
| CN108043183A (en) | A kind of equipment for treating industrial waste gas | |
| CN207755970U (en) | Processing corn hydrolysis prepares the device of inositol process waste gas | |
| CN201643930U (en) | Waste gas purification apparatus | |
| CN207203851U (en) | A kind of Peculiar Odor Treatment System at amino acids production scene | |
| CN208340464U (en) | A kind of cultivation emission-control equipment | |
| CN208727176U (en) | A kind of processing unit and system of dead livestock and poultry foul smell | |
| CN208809764U (en) | Sludge drying exhaust treatment system | |
| CN203437019U (en) | Acid gas recovery tower | |
| CN207734823U (en) | A kind of spray washing system for sludge drying tail gas processing | |
| CN207102292U (en) | A kind of two level acid mist absorptive purifying device | |
| CN206549449U (en) | One kind is accelerated the ripening fermentation waste gas processing unit | |
| CN209989290U (en) | Boron trifluoride complex purification treatment device | |
| CN203648315U (en) | Energy-saving demisting thermal coupled type washing tower system | |
| CN211487140U (en) | Breed exhaust-gas treatment equipment | |
| CN104888592B (en) | Leather-making waste water eliminating malodours from gases system and method | |
| CN209348399U (en) | The fountain processing unit of tung oil squeezing exhaust gas | |
| CN207886954U (en) | A kind of printing emission-control equipment | |
| CN206152604U (en) | Organic waste gas integrated treating equipment | |
| CN207755971U (en) | Gas Photolytic deodorization equipment for slaughterhouse |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |