CN109589768A - The processing method of fish powder waste gases - Google Patents
The processing method of fish powder waste gases Download PDFInfo
- Publication number
- CN109589768A CN109589768A CN201811552815.5A CN201811552815A CN109589768A CN 109589768 A CN109589768 A CN 109589768A CN 201811552815 A CN201811552815 A CN 201811552815A CN 109589768 A CN109589768 A CN 109589768A
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- spray equipment
- gas
- waste gases
- ozone
- powder waste
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- 239000002912 waste gas Substances 0.000 title claims abstract description 77
- 239000000843 powder Substances 0.000 title claims abstract description 74
- 241000251468 Actinopterygii Species 0.000 title claims abstract description 69
- 238000003672 processing method Methods 0.000 title claims abstract description 19
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 124
- 239000007789 gas Substances 0.000 claims abstract description 124
- 239000007921 spray Substances 0.000 claims abstract description 123
- 238000010521 absorption reaction Methods 0.000 claims abstract description 15
- 238000001816 cooling Methods 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims abstract description 10
- 235000019645 odor Nutrition 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 claims description 23
- 238000002156 mixing Methods 0.000 claims description 23
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 17
- 229910052760 oxygen Inorganic materials 0.000 claims description 17
- 239000001301 oxygen Substances 0.000 claims description 17
- 238000011084 recovery Methods 0.000 claims description 15
- 238000001035 drying Methods 0.000 claims description 13
- 238000007710 freezing Methods 0.000 claims description 10
- 230000008014 freezing Effects 0.000 claims description 10
- 235000019733 Fish meal Nutrition 0.000 claims description 9
- 239000004467 fishmeal Substances 0.000 claims description 9
- 238000012545 processing Methods 0.000 claims description 6
- 230000008676 import Effects 0.000 claims description 3
- 238000012797 qualification Methods 0.000 claims description 3
- 238000005507 spraying Methods 0.000 claims description 2
- 238000004332 deodorization Methods 0.000 abstract description 16
- 230000000694 effects Effects 0.000 abstract description 8
- 230000035943 smell Effects 0.000 abstract description 8
- 238000012423 maintenance Methods 0.000 abstract description 7
- 230000008901 benefit Effects 0.000 abstract description 6
- 238000004140 cleaning Methods 0.000 abstract description 6
- 239000003205 fragrance Substances 0.000 abstract description 6
- 239000000126 substance Substances 0.000 abstract description 5
- 230000001590 oxidative effect Effects 0.000 abstract description 4
- 150000003384 small molecules Chemical class 0.000 abstract description 2
- 230000003647 oxidation Effects 0.000 description 10
- 238000007254 oxidation reaction Methods 0.000 description 10
- 230000001877 deodorizing effect Effects 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 239000000523 sample Substances 0.000 description 7
- HGWOWDFNMKCVLG-UHFFFAOYSA-N [O--].[O--].[Ti+4].[Ti+4] Chemical compound [O--].[O--].[Ti+4].[Ti+4] HGWOWDFNMKCVLG-UHFFFAOYSA-N 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 230000001699 photocatalysis Effects 0.000 description 5
- 238000007146 photocatalysis Methods 0.000 description 5
- 150000002500 ions Chemical class 0.000 description 4
- 238000005070 sampling Methods 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000002781 deodorant agent Substances 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- 238000005215 recombination Methods 0.000 description 2
- 230000006798 recombination Effects 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000005276 aerator Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000001413 cellular effect Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011897 real-time detection Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000004408 titanium dioxide Substances 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/75—Multi-step processes
-
- 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
-
- 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
- B01D53/1425—Regeneration of liquid absorbents
-
- 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
- B01D53/38—Removing components of undefined structure
-
- 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
- B01D53/76—Gas phase processes, e.g. by using aerosols
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/10—Oxidants
- B01D2251/104—Ozone
-
- 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
- B01D2258/0275—Other waste gases from food processing plants or kitchens
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Dispersion Chemistry (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
- Treating Waste Gases (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
Abstract
A kind of processing method of fish powder waste gases, by following steps: fish powder waste gases are first entered in condenser to the temperature for be cooled to setting;Then fish powder waste gases after cooling are entered in spray equipment lower lumen by pipeline, mixed with the ozone gas entered in spray equipment lower lumen in ozone generator and carries out oxygenolysis;Fish powder waste gases in spray equipment lower lumen after oxygenolysis flow up, then further remove odors through spray liquid spray-absorption in spray equipment;Fish powder waste gases up to standard are discharged at the top of spray equipment finally by blower.The advantage is that: the substance for generating stink and other smells can be decomposed rapidly using the strong oxidizing property of ozone, scentless small-molecule substance is generated, removes odorant contained by fish powder waste gases, good deodorization effect;Deodorization cost is extremely low;Ozone generator hardly needs cleaning maintenance.
Description
Technical field
The present invention relates to a kind of exhaust gas treatment technology, a kind of especially processing method of fish powder waste gases.
Background technique
Application No. is a kind of middle promulgateds by the State Council of CN201811020857.4 entitled " fish powder waste gases processing unit " for existing one kind
Bright patent application discloses a kind of fish powder waste gases processing unit, the shell of rectangle is presented including cross section, one end of shell is equipped with
Air inlet pipe, other end are equipped with escape pipe, and it is single that the inside of shell is successively arranged several groups oxidation between air inlet pipe to escape pipe
First one and one group of oxidation unit two, group oxidation unit one include titanium dioxide plate module and ultraviolet lamp modules, titanium dioxide titanium plate
Module includes four pieces of titanium dioxide titanium plates, and four pieces of titanium dioxide titanium plates are detachably arranged on four inner sidewalls of shell, ultraviolet radiator
Module includes fixed frame and ultraviolet lamp, and several ultraviolet lamps are equipped in fixed frame, and oxidation unit two includes fixed frame and titanium dioxide
Titanium net, fixed frame is interior to be equipped with titanium dioxide titanium net, and the outer wall of shell is equipped with ozone generator, the ozone delivery outlet of ozone generator
It is connected to by ozone delivery pipe with the inside of shell, is provided with check valve in ozone delivery pipe.The invention is imitated with exhaust-gas treatment
The good advantage of fruit.However, the exhaust treatment efficiency of the device is low, therefore the structure of the device also needs to be further improved.
Summary of the invention
The technical problem to be solved by the present invention is to a kind of sufficiently removal fish meal is provided for above-mentioned state of the art
Exhaust gas stink, exhaust treatment efficiency is high, the processing method of the fish powder waste gases of high treating effect.
The technical scheme of the invention to solve the technical problem is: the processing method of this fish powder waste gases, feature
It is: by following steps:
One, fish powder waste gases are first entered in condenser to the temperature for be cooled to setting;
Two, then fish powder waste gases after cooling are entered in spray equipment lower lumen by pipeline, and from ozone
The ozone gas entered in spray equipment lower lumen in generator mixes and carries out oxygenolysis;
Three, the fish powder waste gases in spray equipment lower lumen after oxygenolysis flow up, then through in spray equipment
Spray liquid spray-absorption further removes odors;
Four, fish powder waste gases up to standard are discharged at the top of spray equipment finally by blower.
As an improvement, in step 2, by fish powder waste gases after cooling in blending tank first and in ozone generator
Ozone gas all the way carry out oxygenolysis, then the fish powder waste gases in blending tank after oxygenolysis are entered into spray by pipeline
Oxygenolysis is carried out again with the ozone gas in ozone generator in the lower lumen of shower device.
Be further improved, the spray equipment have it is N number of, N number of spray equipment be composed in series, the lower part of each spray equipment
It is connected respectively by pipeline with the ozone gas in ozone generator in inner cavity, after first spray equipment oxygenolysis
Fish powder waste gases are transported in the lower lumen of second spray equipment by pipeline, with the ozone gas in second spray equipment
The further oxygenolysis of body and spray, and so on, through detecting, by fish powder waste gases from the top of a spray equipment of qualification up to standard
Portion's discharge, the N are the natural number greater than 1.
As an improvement, the spray equipment includes shell, the spray portion of circulated sprinkling fish powder waste gases, gas supply part, filter house
With circulating pump, fish powder waste gases import is arranged in the lower part of the housing, and fish powder waste gases outlet is arranged in case top, the spray tube in spray portion
Positioned at the top of housing cavity, the recovery pond and gas supply part in spray portion are located at the bottom of housing cavity, the gas supply part and ozone
Delivery pipe is connected, and the gas outlet of gas supply part is located in recovery pond, and the recovery pond is connected by circulating pump with filter house.
It is further improved, the filter house and circulating pump are arranged in hull outside, and the filter house is with circulating pump by wearing
The pipeline for crossing shell is connected with recovery pond.
As an improvement, the ozone generator includes oxygenerator, the oxygenerator includes the air being sequentially communicated
The outlet of compressor, the first gas tank, drying machine, oxygenerator and the second gas tank, second gas tank is connected with ozone generator.
It is further improved, the drying machine includes freezing type drier and absorption drier, the freezing type drier
It is connected with each other with absorption drier, the freezing type drier is connected with the first gas tank, the absorption drier and system
Oxygen machine is connected;The air compressor is oilless air compressor.
As an improvement, being provided with pressure detecting table on the blending tank, the pressure detecting table passes through route and report
Alert device is connected.
As an improvement, being provided with the check valve for preventing gas backflow on the ozone transport conduit of ozone generator.
The present invention solves another technical solution used by above-mentioned technical problem are as follows: the processing method of this fish powder waste gases,
It is characterized by: by following steps:
One, fish powder waste gases are first first entered in condenser to the temperature for be cooled to setting;
Two, by air by the air compressor that is sequentially communicated, the first gas tank, drying machine, after oxygenerator and the second gas tank
Dry oxygen is generated, the oxygen of the drying is passed through in ozone generator, ozone gas is made, by fish meal after cooling
Exhaust gas is entered in blending tank by pipeline, in ozone generator enter blending tank inner cavity ozone gas mix and into
Row oxygenolysis;
Three, the gas after oxygenolysis is passed through from the mixed gas outlet of blending tank to the lower lumen of spray equipment
In, by N number of, N number of spray equipment is composed in series the spray equipment of use, and the gas after oxygenolysis is by pipeline through the first blower
From the lower lumen that the exhaust gas inlet of first spray equipment enters first spray equipment, the gas after oxygenolysis is upward
It flows, spray liquid absorbs the peculiar smell of the gas after further removal oxygenolysis in first spray equipment, by single treatment
Gas from the top of first spray equipment by pipeline enter second spray equipment lower lumen in, carry out secondary spray
Leaching processing, and so on, the gas handled by N-1 times carries out n-th spray process in the last one spray equipment, described
N is the natural number greater than 1;
Four, fish powder waste gases are discharged from the top of the last one spray equipment finally by the second blower.
Compared with the prior art, the advantages of the present invention are as follows: generation stink can be decomposed rapidly using the strong oxidizing property of ozone
And the substance of other smells, scentless small-molecule substance is generated, odorant contained by fish powder waste gases is removed, it is environmentally protective, it removes
It is smelly high-efficient, good deodorization effect;Ozone oxidation is carried out while spraying to fish powder waste gases, off-gas oxidizing is abundant, without additional
Ozone treatment room, save space, also further speed up exhaust-gas treatment speed;Producing ozone is directly to utilize air for raw material,
It is generated by oxygen purification, then with high-voltage electric shock, deodorization cost is extremely low;Due to exhaust gas discord ozone generator contact, ozone hair
Raw device hardly needs cleaning maintenance, reduces the working strength of worker, extends the service life of ozone generator;In addition to power supply, it is not necessarily to
Other cost inputs, ozone devices access production line, so that spray equipment is not necessarily to acid & alkali liquid, not only save money, it is often more important that make
Obtaining wastewater treatment becomes to be more easier, and mitigates fish meal company water process pressure while reducing pollution;In conjunction with shell and tube condenser,
A series of deodorizing waste gas treating equipments such as the spray equipment of fish powder waste gases, deodorizing effect is significant, reaches national waste gas emission standard.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the embodiment of the present invention;
Fig. 2 is the structural schematic diagram that spray equipment is in another angle in Fig. 1.
Specific embodiment
The present invention will be described in further detail below with reference to the embodiments of the drawings.
As depicted in figs. 1 and 2, the processing method of the fish powder waste gases of the present embodiment, by following steps:
One, fish powder waste gases are first entered in condenser 6 to the temperature for be cooled to setting;
Two, then fish powder waste gases after cooling are entered in spray equipment lower lumen by pipeline, and from ozone
The ozone gas entered in spray equipment lower lumen in generator 1 mixes and carries out oxygenolysis;
Three, the fish powder waste gases in spray equipment lower lumen after oxygenolysis flow up, then through in spray equipment
Spray liquid spray-absorption further removes odors;
Four, fish powder waste gases up to standard are discharged at the top of spray equipment finally by blower.
In step 2, by fish powder waste gases after cooling in blending tank 2 first with it is smelly all the way in ozone generator 1
Carrier of oxygen carries out oxygenolysis, then the fish powder waste gases in blending tank 2 after oxygenolysis are entered spray equipment by pipeline
Lower lumen in ozone gas in ozone generator 1 carry out oxygenolysis again.Spray equipment have it is N number of, it is N number of
Spray equipment is to be composed in series, and passes through the ozone in pipeline and ozone generator 1 in the lower lumen of each spray equipment respectively
Gas is connected, and the fish powder waste gases after first spray equipment oxygenolysis are transported to second spray equipment by pipeline
Lower lumen in, in second spray equipment the further oxygenolysis of ozone gas and spray, and so on, through examining
It surveys, fish powder waste gases is discharged from the top of a spray equipment of qualification up to standard, the N is the natural number greater than 1.Blending tank 2
It is also possible to help mixed machine for hollow general tanks, fish powder waste gases are mixed with ozone in blending tank 2 and pre-processed, and ozone is by portion
Divide fish powder waste gases oxidation, removes stink.The specific structure of ozone generator 1 belongs to well-known technique, therefore is not described further in detail.Helping mixed machine is
A kind of very common gas mixing apparatus, therefore be also not described further in detail.
Spray equipment includes shell 4, the spray portion of circulated sprinkling fish powder waste gases, gas supply part 42, filter house 43 and circulating pump
44, fish powder waste gases import setting is in 4 lower part of shell, and fish powder waste gases outlet setting is in 4 top of shell, the spray tube in spray portion 41
In the top of housing cavity, the recovery pond 45 in spray portion and gas supply part 42 are located at the bottom of housing cavity, the gas supply part 42 and
Ozone delivery pipe 11 is connected, and the gas outlet of gas supply part 42 is located in recovery pond 45, the recovery pond 45 by circulating pump 44 with
Filter house 43 is connected.The filter house 43 is arranged with circulating pump 44 in hull outside, and the filter house 43 and circulating pump 44 are logical
The pipeline crossed across shell is connected with recovery pond 45.Ozone generator 1 includes oxygenerator, the oxygenerator include according to
The air compressor 5 of secondary connection, the first gas tank 51, drying machine, oxygenerator 54 and the second gas tank 55, second gas tank 55 go out
Mouth is connected with ozone generator 1.Drying machine includes freezing type drier 52 and absorption drier 53, and the freezing type is dry
Machine 52 and absorption drier 53 are connected with each other, and the freezing type drier 52 is connected with the first gas tank 51, the absorption type
Drying machine 53 is connected with oxygenerator 54;The air compressor 5 is oilless air compressor.On the blending tank 2
It is provided with pressure detecting table, the pressure detecting table is connected by route with alarm.It is conveyed in the ozone of ozone generator 1
The check valve 13 for preventing gas backflow is provided on pipeline 11.Delivery branch pipe 12, conveying branch are provided on ozone transport conduit 11
Check valve 13 is also equipped on pipe 12, delivery branch pipe 12 is connected with blending tank 2.Gas supply part 42, spray portion, filter house 43 follow
Ring pump 44, the specific structure of recovery pond 45 belong to well-known technique, gas supply part 42, spray portion, filter house 43, circulating pump 44, recycling
The connection type in pond 45 also belongs to well-known technique, therefore is not described in detail.
Another processing method of the fish powder waste gases of embodiment, by following steps:
One, fish powder waste gases are first entered in condenser 6 to the temperature for be cooled to setting;
Two, air is passed through to the air compressor 5 being sequentially communicated, the first gas tank 51, drying machine, oxygenerator 54 and the second gas
Dry oxygen is generated after tank 55, the oxygen of the drying is passed through in ozone generator 1, ozone gas is made, after cooling
Fish powder waste gases entered in blending tank 2 by pipeline, in ozone generator 1 enter blending tank inner cavity ozone gas
It mixes and carries out oxygenolysis;
Three, the gas after oxygenolysis is passed through from the mixed gas outlet of blending tank 2 to the lower lumen of spray equipment
In, by N number of, N number of spray equipment is composed in series the spray equipment of use, and the gas after oxygenolysis is by pipeline through the first blower
31 from the lower lumen that the exhaust gas inlet of first spray equipment enters first spray equipment, gas after oxygenolysis to
Upper flowing, spray liquid absorbs the peculiar smell of the gas after further removal oxygenolysis in first spray equipment, by once locating
The gas of reason carries out secondary from the lower lumen that the top of first spray equipment enters second spray equipment by pipeline
Spray process, and so on, the gas handled by N-1 times carries out n-th spray process, institute in the last one spray equipment
Stating N is the natural number greater than 1;
Four, fish powder waste gases are discharged from the top of the last one spray equipment finally by the second blower 32.
Ozone generator 1 can be single hose and be also possible to cellular, be provided with intelligent control in ozone delivery pipe 11
Device, intelligent controller keep the ozone in ozone delivery pipe 11 with 10~2000g/hr, 15~120g/m3Speed output.
Air is passed through in freezing type drier 52 and absorption drier 53 and is removed after the compression of air compressor 5
Water is dry, then comes out oxygen extraction in air by oxygenerator 54, then oxygen is passed through in ozone generator 1, enters
The air of ozone generator 1 contains the oxygen of high level, this partial oxidation is decomposed by high voltage, and atom recombination generates ozone,
Air is followed to enter ozone delivery pipe 11.And ozone delivery pipe 11 can be passed into blending tank and spray equipment, mixed
It closing in tank and spray equipment, ozone and fish powder waste gases sufficiently Rapid contact and are uniformly mixed, by the extremely short time, one to two
Second, the odorant in fish powder waste gases is almost clean by ozone degradation, and clean gas enters gas exhaust piping at this time, harmless up to standard
Drain into atmosphere.
Certainly, spray equipment can also be replaced using eddy flow tower, in order to which ozone can be uniformly and quickly mixed with fish powder waste gases
It closes, gas supply part 42 will be arranged in every spray equipment.It, cannot be by ozone treatment in view of spray liquid is the recirculated water being recycled
Particulate matter can constantly reduce the effect of spray equipment, we have installed filter house 43 additional to each spray equipment, be equipped with circulating pump
To guarantee the clean-up performance of recirculated water.
Check valve 13 is provided on the output channel of ozone generator 1, fish powder waste gases discord ozone generator 1 contacts, smelly
Oxygen Generator 1 hardly needs cleaning maintenance, and life of product is long, and performance is stablized.Occupied area very little, deodorant generation module peace
Dress space requirement is very low, and installation site is flexible, since fish powder waste gases are not directly contacted with ozone generator 1, therefore is mounted on idle
Position, maintenance is low, in addition to power supply, it is convenient for management almost without other costs, only need to power on, ozone
Generator 1 uses stainless steel chassis design, and more attractive, anticorrosion oxidative resistance is stronger, and the concentration of ozone generator 1 is adjustable,
Different zones are facilitated to require using concentration, it is energy-efficient.
Deodorizing methods there are many in industrial deodorization, but it is all undesirable,
First, for environmental angle.For deodorancy protocol by taking " active carbon adsorption " as an example, this kind of processing sides
Case can all generate secondary pollution, and factory also needs to handle this part secondary pollution, can bring other negative impacts;
Second, for factory's angle.For deodorancy protocol by taking " microbial deodorant method " as an example, each investment all can
A large amount of area is occupied, but also wants huge maintenance fund, for the factory for pursuing economic benefit, this problem is difficult to
Receive;
Third, for worker's angle.For deodorancy protocol by taking " photocatalysis deodorization " as an example, although this scheme is taken up an area
Area is small, and maintenance is convenient, but undeniable is that, due to the limitation of current material science, there is most for such equipment
Big drawback, that is, equipment component is frequently replaced, while in equipment operation, the cleaning of equipment is frequently harsh,
In the case where not considering equipment component damage, equipment cleaning inside is also kept, in people-oriented modern plant, this side
Case has exposed its defect.
Our company carries out exhaust air deodorization using the processing unit of this fish powder waste gases and solves the above problem.
Initial Research Thinking seeks to solve the problems, such as above-mentioned third, because first and Second Problem are at present all
Through there are many can also reduce cost while scheme can accomplish to thoroughly remove pollution, for example, it is " photocatalysis deodorization " and " high
Energy ion deodorization " scheme, what is be most difficult to only is exactly people-oriented problem.
By largely visiting and learning, it has been found that the present treatment device of use, it can be by deodorizing device and exhaust-gas treatment
Portion keeps apart, and thus largely solves problem described above.Certainly, isolation herein is said exhaust gas
Keep apart, but deodorizing device is isolated from whole exhaust-gas treatment line, entire deodorizing device itself does not participate in directly
The process of exhaust air deodorization.And if the selection from " photocatalysis deodorization " and " energetic ion deodorization ", it is clear that be all unrealistic
, because if both schemes just can not all remove the odorant in removing exhaust gas if exhaust gas is not crossed from equipment.Through excessive
Amount analysis, it has been found that either " photocatalysis deodorization " still " energetic ion deodorization ", they have a common mode to remove
It is smelly, and this mode does not exactly need exhaust gas and passes through from the device, here it is " ozone deodorizings ".
In general, all containing a large amount of oxygen in air or exhaust gas, these oxygen are in " photocatalysis " and " energetic ion is made
Under " ozone can be generated, and ozone has very strong oxidation to exhaust gas, can almost aoxidize 90% or more malodorant
Matter is particularly effective fish powder waste gases, and the generation of ozone can just be kept apart with production line completely, while can solve first again
A environmental issue and second economical efficiency.
Cardinal principle: air water removal (subsidiary cooling effect) oil removing --- air oxygen --- oxygen ozone --- ozone
Fish powder waste gases are aoxidized, overall process uses PLC Automatic Detection and Control whole equipment.
Process explanation: air is compressed by air compressor, then passes to absorption drier and cooled is dry
After machine is removed water, into the first gas tank, at this point, the compressed air of the first gas tank be it is more dry, be then passed into
In ozone generator, the oxygen of high level is contained into the air of ozone generator, this partial oxidation is decomposed by high voltage, former
Son recombination, produces ozone, and ozone follows air to enter ozone delivery pipe again.And ozone delivery pipe can separate delivery branch pipe,
Ozone is passed through blending tank by delivery branch pipe, and wherein, ozone and exhaust gas sufficiently Rapid contact and are uniformly mixed, process one to two
Second time, the ozone in exhaust gas is almost completely depleted, and exhaust gas enters in spray equipment at this time, and spray equipment bottom has one
Ozone is passed through inside spray equipment in recovery pond 45 by a recovery pond 45 by an aerator, and be diffused into exhaust gas and
In recirculated water, after the spray equipment for configuring respective numbers according to the actual situation, the odorant in exhaust gas is almost by ozone oxidation
Completely, clean gas enters gas exhaust piping at this time, and harmless qualified discharge enters atmosphere.In view of exhaust gas constantly enters recirculated water,
The effect of spray equipment can cannot be constantly reduced by the particulate matter of ozone treatment, we have installed one additional to each spray equipment
Filter is equipped with circulating pump 44 to guarantee the clean-up performance of recirculated water.It is shown according to engineering real case, which has very much
Effect.
Science control: during daily ozone deodorizing, since raw material fingerling class is changing, while daily, yield is also not
One steady state value, this results in exhaust gas production and exhaust gas stink substances type and concentration all constantly changing, so if
Laissez-faire ozone devices generate ozone daily with steady state value, then being possible to occur ozone excessive leakage causes to aggravate to pollute,
After all it is well known that breathing excessive ozone on humans or other biological all adversely affects.In view of this, we introduce again
A whole set of ozone detection system, which not only can be with the final effect of real-time detection exhaust air deodorization, but also this can be believed
PLC system number is fed back to, PLC carries out global optimization adjustment to ozone generation module again, so that the yield of ozone remains
In an optimal state.
Actual installation method is as follows:
1, before all operations progress, need to prepare 1,10G model machine, probe tube one, sample length of tube is according to actual bit
Depending on setting, anemobiagraph 2, wherein 1 it is spare, engineer 2, be each responsible for operate and measure, fish meal producer responsible person it is many
In 3 people, deodorizing effect is assert, fish meal factory man unskilled labourer it is several, assist measurement;
2, engineer is attached exhaust gas sampling pipeline, and sample position takes last shell and tube condenser or air cooler
First fan outlet later, general pipeline wind speed when recording sampling near sampling, while the wind speed in the probe tube is recorded,
The caliber of general pipeline and probe tube is also recorded, is connected at the exhaust gas inlet of 10G model machine to calculate the outlet of air quantity probe tube;
3, after engineer confirms that piping connection is complete, corresponding air intake valve is opened in the presence of demander responsible person, opens model machine electricity
Ozone amount knob is threaded at 0G/H by source, while at waste gas outlet, and demander responsible person is asked to confirm exhaust gas by the method for odor
For the fish powder waste gases that probe tube comes, then knob is threaded to 2G/H, 4G/H, 6G/H, 8G/H, 10G/H respectively and (be usually no more than
6G/H), this process whole process needs demander responsible person to confirm, until three people think to smell in exhaust gas without stink
All it is the taste of ozone, ozone amount is adjusted demander personnel and think both to can't smell exhaust gas taste or can't smell toward small adjustment at this time
Ozone taste records ozone output valve at this time;
Note: it is a little 1., during this to need to prepare ground coffee, adjusts for smell, because hearing exhaust gas always, nose meeting
Failure;
2., due to individual differences, it is different to fish powder waste gases susceptibility, so ten million cannot only allow one or two of people to confirm
Exhaust-gas treatment degree is preferably formed with 5 people or more and participates in assessment if conditions permit, to guarantee that test is accurate.
4, after completing process as described above, exhaust gas inlet valve is closed, closes power supply, restores sampling scene;
5, by calculating, total configuration of ozone production line is calculated, inquires manufacturer, fish meal company when measurement
Yield, raw material condition and other factors, after integrating nearly all factor that can be considered, so that it may deduce the fish meal producer
Then maximum ozone demand when at full capacity puts corresponding surplus to the numerical value, yield customization can be completed.
It will be apparent that this deodorization process, there is following three advantages:
1, odorant contained by all fish powder waste gases can be almost removed, it is effectively reliable for environmental angle;
2, due to exhaust gas discord equipment contact, equipment hardly needs cleaning maintenance, reduces the working strength of worker, simultaneously
Equipment life is very big with respect to other process advantages;
3, in addition to power supply, other cost inputs are not necessarily to, ozone devices access production line, so that spray equipment is not necessarily to soda acid
Liquid not only saves money, it is often more important that so that wastewater treatment becomes to be more easier, mitigates fish meal company Shui Chu while reducing pollution
Manage pressure.
Claims (10)
1. a kind of processing method of fish powder waste gases, it is characterised in that: by following steps:
One, fish powder waste gases are first entered into condenser (6) temperature for carrying out being cooled to setting;
Two, then fish powder waste gases after cooling are entered in spray equipment lower lumen by pipeline, is occurred with from ozone
The ozone gas entered in spray equipment lower lumen in device (1) mixes and carries out oxygenolysis;
Three, the fish powder waste gases in spray equipment lower lumen after oxygenolysis flow up, then through spraying in spray equipment
Liquid spray-absorption further removes odors;
Four, fish powder waste gases up to standard are discharged at the top of spray equipment finally by blower.
2. processing method according to claim 1, it is characterised in that: in step 2, by fish powder waste gases after cooling mixed
It closes in tank (2) and first carries out oxygenolysis with the ozone gas all the way in ozone generator (1), then will be in blending tank (2)
The middle fish powder waste gases after oxygenolysis are entered by pipeline in the lower lumen of spray equipment and from ozone generator (1)
In ozone gas carry out oxygenolysis again.
3. processing method according to claim 2, it is characterised in that: the spray equipment has N number of, and N number of spray equipment is
It is composed in series, is connected respectively by pipeline with the ozone gas in ozone generator (1) in the lower lumen of each spray equipment
Logical, the fish powder waste gases after first spray equipment oxygenolysis are transported in the lower part of second spray equipment by pipeline
In chamber, in second spray equipment the further oxygenolysis of ozone gas and spray, and so on, through detecting, by fish meal
Exhaust gas is discharged from the top of a spray equipment of qualification up to standard, and the N is the natural number greater than 1.
4. processing method according to any one of claims 1 to 3, it is characterised in that: the spray equipment includes shell
(4), the spray portion of circulated sprinkling fish powder waste gases, gas supply part (42), filter house (43) and circulating pump (44), fish powder waste gases import are set
It sets in shell (4) lower part, at the top of shell (4), the spray tube (41) in spray portion is located at housing cavity for fish powder waste gases outlet setting
Top, the recovery pond (45) in spray portion and gas supply part (42) are located at the bottom of housing cavity, the gas supply part (42) and ozone
Delivery pipe (11) is connected, and the gas outlet of gas supply part (42) is located in recovery pond (45), and the recovery pond (45) passes through circulating pump
(44) it is connected with filter house (43).
5. processing method according to claim 4, it is characterised in that: the filter house (43) and circulating pump (44) are arranged
Hull outside, the filter house (43) are connected by passing through the pipeline of shell with recovery pond (45) with circulating pump (44).
6. processing method according to any one of claims 1 to 3, it is characterised in that: the ozone generator (1) includes
Oxygenerator, the oxygenerator include the air compressor (5) being sequentially communicated, the first gas tank (51), drying machine, oxygenerator
(54) with the second gas tank (55), the outlet of second gas tank (55) is connected with ozone generator (1).
7. processing method according to claim 6, it is characterised in that: the drying machine include freezing type drier (52) and
Absorption drier (53), the freezing type drier (52) and absorption drier (53) are connected with each other, and the freezing type is dry
Dry machine (52) is connected with the first gas tank (51), and the absorption drier (53) is connected with oxygenerator (54);The air
Compressor (5) is oilless air compressor.
8. the processing method according to Claims 2 or 3, it is characterised in that: be provided with pressure on the blending tank (2)
Power detects table, and the pressure detecting table is connected by route with alarm.
9. the processing method according to Claims 2 or 3, it is characterised in that: in the ozone delivery pipe of ozone generator (1)
The check valve (13) for preventing gas backflow is provided on road (11).
10. a kind of processing method of fish powder waste gases, it is characterised in that: by following steps:
One, fish powder waste gases are first entered into condenser (6) temperature for carrying out being cooled to setting;
Two, air is passed through to the air compressor (5) being sequentially communicated, the first gas tank (51), drying machine, oxygenerator (54) and second
Gas tank (55) generates dry oxygen afterwards, the oxygen of the drying is passed through in ozone generator 1, ozone gas is made, will be cold
But the fish powder waste gases after are entered in blending tank (2) by pipeline, with the entrance blending tank inner cavity in ozone generator (1)
Ozone gas mixes and carries out oxygenolysis;
Three, the gas after oxygenolysis is passed through from the mixed gas outlet of blending tank (2) into the lower lumen of spray equipment,
By N number of, N number of spray equipment is composed in series the spray equipment of use, and the gas after oxygenolysis is by pipeline through the first blower
(31) gas from the lower lumen that the exhaust gas inlet of first spray equipment enters first spray equipment, after oxygenolysis
It flows up, spray liquid absorbs the peculiar smell of the gas after further removal oxygenolysis in first spray equipment, by primary
The gas of processing carries out two from the lower lumen that the top of first spray equipment enters second spray equipment by pipeline
Secondary spray process, and so on, the gas handled by N-1 times carries out n-th spray process in the last one spray equipment,
The N is the natural number greater than 1;
Four, fish powder waste gases are discharged from the top of the last one spray equipment finally by the second blower (32).
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112915739A (en) * | 2021-01-25 | 2021-06-08 | 中山大学 | Heterogeneous catalytic oxidation processing system of organic waste gas and foul smell waste gas |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1937574A1 (en) * | 1969-07-24 | 1971-02-11 | August Klueber Appbau Und Wass | Removing waste gases containing ozone |
| CN204656302U (en) * | 2015-03-16 | 2015-09-23 | 长沙高新开发区湘麓环保科技有限公司 | A kind of photochemical oxidation deodoration system |
| CN205308111U (en) * | 2015-12-24 | 2016-06-15 | 杭州中兵环保股份有限公司 | Tobacco processing exhaust gas purification device |
| CN207102282U (en) * | 2017-07-06 | 2018-03-16 | 山东海林环保设备工程有限公司 | Peculiar smell deodorization cleaning equipment |
-
2018
- 2018-12-18 CN CN201811552815.5A patent/CN109589768A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1937574A1 (en) * | 1969-07-24 | 1971-02-11 | August Klueber Appbau Und Wass | Removing waste gases containing ozone |
| CN204656302U (en) * | 2015-03-16 | 2015-09-23 | 长沙高新开发区湘麓环保科技有限公司 | A kind of photochemical oxidation deodoration system |
| CN205308111U (en) * | 2015-12-24 | 2016-06-15 | 杭州中兵环保股份有限公司 | Tobacco processing exhaust gas purification device |
| CN207102282U (en) * | 2017-07-06 | 2018-03-16 | 山东海林环保设备工程有限公司 | Peculiar smell deodorization cleaning equipment |
Non-Patent Citations (4)
| Title |
|---|
| 中华人民共和国国家环境保护局: "《中华人民共和国国家标准 GB/T 14675-93空气质量 恶臭的测定 三点比较式臭袋法》", 15 March 1994 * |
| 李凯等编著: "《化工行业大气污染控制》", 31 January 2016, 冶金工业出版社 * |
| 林丽霞等编著: "《牛仔产品艺术加工》", 28 February 2014, 东华大学出版社 * |
| 臧学丽等编著: "《实用发酵工程技术》", 31 January 2017, 中国医药科技出版社 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112915739A (en) * | 2021-01-25 | 2021-06-08 | 中山大学 | Heterogeneous catalytic oxidation processing system of organic waste gas and foul smell waste gas |
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