CN108295628A - A kind of fish meal production low exhaust emission device and application - Google Patents
A kind of fish meal production low exhaust emission device and application Download PDFInfo
- Publication number
- CN108295628A CN108295628A CN201810102552.1A CN201810102552A CN108295628A CN 108295628 A CN108295628 A CN 108295628A CN 201810102552 A CN201810102552 A CN 201810102552A CN 108295628 A CN108295628 A CN 108295628A
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- Prior art keywords
- pipeline
- fish meal
- exhaust gas
- equipment
- pipe
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Classifications
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- 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
- B01D53/32—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 electrical effects other than those provided for in group B01D61/00
-
- 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
- B01D53/002—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 condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/14—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects using gases or vapours other than air or steam, e.g. inert gases
Abstract
The present invention provides a kind of fish meal production low exhaust emission device, is made of collection device, water cooling equipment, air cooler, soda acid washing equipment, sampling plasma processing, burning facility, air drier, the 1st 7 pipeline and digesting apparatus.The problem of apparatus of the present invention are for fish powder waste gases discharge is adjusted equipment combination, improves and design.The present invention makes full use of the high temperature and humidity vapor of boiling, drying to concentrate, concentration second heat is carried out to utilize, then water condensation cooling method cools down exhaust gas, carry out air-cooled reducing temperature twice again, after by soda acid wash dehumidification treatments, then pass through sample plasma treatment, high temperature incineration, so that exhaust gas dimensionless index is less than 2000, discharge exhaust gas is again introduced into air drier, fish meal is dried again using hot wind tail gas.Reasonable design of the present invention, can reach the substantially not outside emission of low emission, repeats effectively to use thermal energy, reaches energy conservation and environmental protection standard, application that can be in fish meal production in low exhaust emission.
Description
Technical field
The invention belongs to field of environment protection, are related to improvement more particularly to a kind of fish meal production low exhaust emission of fish powder waste gases
Device and its application process.
Background technology
It is raw material that fish meal processing, which is using Optimization of Low Value Fish and leftover bits and pieces, passes through thermophilic digestion, squeezing, drying, cooling, crushing etc.
Feed fish meal is made in process.In boiling and drying process link, the vapor of a large amount of high temperature, high humidity is will produce, with dry
Fish internal water after dry together, as direct emission can cause stench object to influence environment in air.
Government pays much attention to environmental protection nearly ten years, is renovated to the exhaust gas discharge of fish meal processing, setting exhaust gas row
Standard is put, although producer's active response state-of-the-nation call, infusion of financial resources addition equipment regulation exhaust gas discharge, because domestic equipment manufactures
Quotient does not know about fish meal production technology, and the adaptability of equipment and correction space are larger, although so exhaust gas regulation effectively, is runed
Costly, energy consumption waste is big, causes production cost significantly raised.My company effectively renovates waste gas pollution control and treatment to reducing energy consumption, perfect
Technique, adjusting device combination are unfolded to inquire into low emission production technology.
Invention content
The object of the present invention is to provide a kind of fish meal to produce low exhaust emission device, by collection device, first pipe, water cooling
Equipment, second pipe, air cooler, third pipeline, soda acid washing equipment, the 4th pipeline, sampling plasma processing, the 5th
Pipeline, burning facility, the 6th pipeline, air drier, the 7th pipeline and digesting apparatus composition；Collection device setting is set in boiling
Standby top, collection device connect water cooling equipment by first pipe, and water cooling equipment connects air cooler by second pipe, air-cooled
Equipment connects soda acid washing equipment by third pipeline, then connects sampling plasma processing, sampling etc. by the 4th pipeline
Plasma processing apparatus plasma treatment includes mainly ozone oxidation equipment and UV photodissociation equipment.Sampling plasma processing passes through
5th pipeline connects burning facility, then connects air drier by the 6th pipeline, and then connecting boiling by the 7th pipeline sets
It is standby., pipeline used and tank material select stainless steel 201, wind turbine material selection fiberglass.
Second object of the present invention is to provide application of the described device in fish meal production in low exhaust emission, by with
Lower step is realized：The fish meal that the inside is placed on first with digesting apparatus boiling generates high temperature and humidity vapor, is filled using collecting
It sets collection to concentrate, carries out concentration second heat and utilize, the gas of generation is cooled down by first pipe by the water condensation of water cooling equipment
Mode cools down exhaust gas, and cooling exhaust gas enters air cooler using second pipe and carries out air-cooled reducing temperature twice, and exhaust gas cooling is made to reach
To 30 DEG C hereinafter, exhaust gas dimensionless index reaches 100,000 or so, which carries out using third pipeline to soda acid washing equipment
Soda acid washes dehumidification treatments, so that exhaust gas dimensionless index is reached 50,000 or so, then enter sampling plasma treatment by the 4th pipeline
Equipment is sampled plasma treatment, and the plasma processing for plasma processing of sampling includes mainly ozone oxidation equipment
With UV photodissociation equipment, burning facility high temperature incineration is entered by the 5th pipeline after processing, burns 800 DEG C or so of central temperature,
300 DEG C of temperature is excluded, outlet exhaust gas dimensionless index is less than 2000, and discharge exhaust gas again passes by the 6th pipeline and enters heated-air drying
Machine is positioned over the fish meal inside digesting apparatus by the 7th pipeline drying using hot wind tail gas is generated, can be achieved to be both low in this way
Not outside emission, repetition effectively use thermal energy, reach energy conservation and environmental protection standard again for discharge.Integral device is connected by various pipelines
It connects, realizes the low emission of exhaust gas in fish meal production process.
The problem of present invention is discharged for fish powder waste gases is adjusted equipment combination, improves production, and design provides a kind of fish
Powder produces low exhaust emission device.It makes full use of the high temperature and humidity vapor of boiling, drying to concentrate, carries out concentration second heat profit
With, then water condensation cooling method cools down exhaust gas, then carries out air-cooled reducing temperature twice, after dehumidification treatments are washed by soda acid, then lead to
Oversampling plasma treatment, high temperature incineration make exhaust gas dimensionless index be less than 2000.In order to reach low emission standard, 300 DEG C
Discharge exhaust gas be again introduced into air drier, using hot wind tail gas dry fish meal, can reach in this way low emission substantially not outward
Emission repeats effectively to use thermal energy, reaches energy conservation and environmental protection standard.The present invention is in elution plus plasma catalytic degradation is combined
Exhaust gas is handled, it is better；Integral type closed circulation processing system simultaneously, several non-exhaust emissions；It is recycled to steaming by hot exhaust gas
Equipment is boiled, the secondary use of thermal energy is realized, improves heat energy efficiency, save cost.
Description of the drawings
Fig. 1 is apparatus of the present invention structural schematic diagram.
Specific implementation mode
The present invention is further described in conjunction with the accompanying drawings and embodiments.
Embodiment 1
Referring to Fig. 1, a kind of fish meal produces low exhaust emission device, by collection device 1, first pipe 2, water cooling equipment 3, the
Two pipelines 4, air cooler 5, third pipeline 6, soda acid washing equipment 7, the 4th pipeline 8, sampling plasma processing the 9, the 5th
Pipeline 10, burning facility 11, the 6th pipeline 12, air drier 13, the 7th pipeline 14 and digesting apparatus 16 form, collection device
1 setting connects water cooling equipment 3 in 16 top of digesting apparatus, collection device 1 by first pipe 2, and water cooling equipment 3 passes through second
Pipeline 4 connects air cooler 5, and air cooler 5 connects soda acid washing equipment 7 by third pipeline 6, then is connected by the 4th pipeline 8
Sampling plasma processing 9 is connect, the plasma treatment for plasma processing 9 of sampling includes mainly ozone oxidation equipment and UV
Photodissociation equipment, sampling plasma processing 9 select HHCR-3000.Plasma processing 9 of sampling is connected by the 5th pipeline 10
Burning facility 11 is connect, then air drier 13 is connected by the 6th pipeline 12, digesting apparatus is then connected by the 7th pipeline 14
16.The pipeline and tank material of selection select stainless steel 201, wind turbine material selection fiberglass.
Embodiment 2
High temperature and humidity vapor is generated first with 16 boiling 100kg fish meal 15 of digesting apparatus, is collected using collection device 1
It concentrates, carries out concentration second heat and utilize, then gas is cold by the water condensation cooling method of water cooling equipment 3 by first pipe 2
But exhaust gas, cooling exhaust gas carry out air-cooled reducing temperature twice using second pipe 4 into air cooler 5, and exhaust gas cooling is made to reach 29
DEG C, exhaust gas dimensionless index reaches 100,000, and but exhaust gas is removed using third pipeline 6 to the progress soda acid washing of soda acid washing equipment 7
Wet process makes exhaust gas dimensionless index reach 50,000, then enters sampling plasma processing 9 by the 4th pipeline 8 and be sampled
Then plasma treatment enters burning facility 11 by the 5th pipeline 10 and carries out high temperature incineration, burns 802 DEG C of central temperature, row
Except 298 DEG C of temperature, outlet exhaust gas dimensionless index 1980, the exhaust gas of discharge again passes by the 6th pipeline 12 and enters air drier
13, the fish meal 15 being positioned over inside digesting apparatus 16 is dried by the 7th pipeline 14 using hot wind tail gas is generated, can reach in this way
The not outside emission of low emission repeats effectively to use thermal energy, reaches energy conservation and environmental protection standard.Integral device is connected by various pipelines
It connects so that the low emission of exhaust gas in fish meal production process.The exhaust gas main component in each stage composes Buddhist nun by third party and tests company
Detection, the results are shown in Table 1.As can be seen that after air-cooled, lye spray, plasma treatment, acrolein concentrations reduce 95%,
Concentration of hydrogen sulfide reduces 98.9%, and ammonia reduces 89.7%, and trimethylamine reduces 85.4%, and non-methane reduces 54.2%.
And largely enter boiler digesting apparatus 16 again carries out next cycle to this final portion, realizes zero substantially
Discharge.
Table 1
Embodiment 3 (problem leads to embodiment 2, changes referring to embodiment 2)
High temperature and humidity vapor is generated first with 16 boiling 150kg fish meal 15 of equipment, is collected and is concentrated using collection device,
Concentration second heat is carried out to utilize, then gas cools down exhaust gas by first pipe 2 by 3 water condensation cooling method of water cooling equipment,
Cooling exhaust gas carries out air-cooled reducing temperature twice using second pipe 4 into air cooler 5, so that exhaust gas cooling is reached 31 DEG C, exhaust gas
Dimensionless index reaches 100,000, and gas carries out soda acid using second pipe 6 to soda acid washing equipment 7 and washes dehumidification treatments, makes
Exhaust gas dimensionless index reaches 50,000, then enters sampling plasma processing 9 by the 4th pipeline 8 and be sampled at plasma
11 high temperature incineration of burning facility is entered by the 5th pipeline 10 after reason, burns 798 DEG C of central temperature, 301 DEG C of temperature is excluded, goes out
Gas exhaust gas dimensionless index 1990.Discharge exhaust gas again passes by the 6th pipeline 12 and enters air drier 13, utilizes generation hot wind
Tail gas dries fish meal 15 by the 7th pipeline 14, can reach the not outside emission of low emission in this way, repeats effectively to use thermal energy,
Reach energy conservation and environmental protection standard.Integral device is connected by various pipelines so that the low emission of exhaust gas in fish meal production process.Processing
Each stage exhaust gas composes Buddhist nun by third party and tests company's detection, the results are shown in Table 2.As can be seen that sprayed by air-cooled, lye, etc.
After ion processing, acrolein concentrations reduce 96.1%, and concentration of hydrogen sulfide reduces 99.3%, and ammonia reduces 88.6%, front three
Amine reduces 89.1%, and non-methane reduces 54.8%.And this final portion largely enters boiler steaming again
It boils equipment 16 and carries out next cycle, realize zero-emission substantially.(preferably having a section explanatory note to testing result)
Table 2
。
Claims (5)
1. a kind of fish meal produces low exhaust emission device, which is characterized in that set by collection device (1), first pipe (2), water cooling
Standby (3), second pipe (4), air cooler (5), third pipeline (6), soda acid washing equipment (7), the 4th pipeline (8), sampling etc.
Plasma processing apparatus (9), the 5th pipeline (10), burning facility (11), the 6th pipeline (12), air drier (13), the 7th pipe
Road (14) and digesting apparatus (16) composition, at the top of the digesting apparatus (16), collection device (1) passes through for collection device (1) setting
One pipeline (2) connects water cooling equipment (3), and water cooling equipment (3) connects air cooler (5), air cooler by second pipe (4)
(5) soda acid washing equipment (7) is connected by third pipeline (6), then sampling plasma processing is connected by the 4th pipeline (8)
(9), sampling plasma processing (9) connects burning facility (11) by the 5th pipeline (10), then passes through the 6th pipeline (12)
Air drier (13) is connected, digesting apparatus (16) is then connected by the 7th pipeline (14).
2. a kind of fish meal according to claim 1 produces low exhaust emission device, which is characterized in that sampling plasma treatment
Equipment (9) plasma treatment includes ozone oxidation equipment and UV photodissociation equipment.
3. a kind of fish meal according to claim 1 produces low exhaust emission device, which is characterized in that pipeline and case used
Body material selection stainless steel 201, wind turbine material selection fiberglass.
4. a kind of fish meal production low exhaust emission device answering in low exhaust emission in fish meal production described in claim 1
With.
5. application according to claim 4, which is characterized in that realized by following steps：First with digesting apparatus
(16) boiling is placed on fish meal (15) the generation high temperature and humidity vapor of the inside, is collected and is concentrated using collection device (1), carried out dense
Contracting second heat utilizes, and the gas of generation, which is cooled down by first pipe (2) by the water condensation cooling method of water cooling equipment (3), to give up
Gas, cooling exhaust gas enter air cooler (5) using second pipe (4) and carry out air-cooled reducing temperature twice, and exhaust gas cooling is made to reach 30
DEG C hereinafter, exhaust gas dimensionless index reaches 100,000, which carries out acid using third pipeline (6) to soda acid washing equipment (7)
Buck removes wet process, so that exhaust gas dimensionless index is reached 50,000, then enter sampling plasma treatment by the 4th pipeline (8) and set
Standby (9) are sampled plasma treatment, and sampling plasma processing (9) includes mainly that ozone oxidation equipment and UV photodissociation are set
It is standby, burning facility (11) high temperature incineration is entered by the 5th pipeline (10) after processing, burns 800 DEG C of central temperature, excludes temperature
300 DEG C of degree, outlet exhaust gas dimensionless index are less than 2000, and discharge exhaust gas again passes by the 6th pipeline (12) and enters air drier
(13), real using generation hot wind tail gas by the dry fish meal (15) being positioned over inside digesting apparatus (16) of the 7th pipeline (14)
The low emission of exhaust gas in existing fish meal production process.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810102552.1A CN108295628A (en) | 2018-02-01 | 2018-02-01 | A kind of fish meal production low exhaust emission device and application |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810102552.1A CN108295628A (en) | 2018-02-01 | 2018-02-01 | A kind of fish meal production low exhaust emission device and application |
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| Publication Number | Publication Date |
|---|---|
| CN108295628A true CN108295628A (en) | 2018-07-20 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810102552.1A Pending CN108295628A (en) | 2018-02-01 | 2018-02-01 | A kind of fish meal production low exhaust emission device and application |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109045932A (en) * | 2018-09-20 | 2018-12-21 | 岭商（浙江）生物科技有限公司 | A kind of exhaust treatment system and its treatment process of fish meal |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101185820A (en) * | 2007-08-24 | 2008-05-28 | 陈昆柏 | Method and device for fathering fish powder waste gases |
| CN105698521A (en) * | 2016-03-30 | 2016-06-22 | 广东环葆嘉节能科技有限公司 | Hot-air drying system and method |
| CN205516946U (en) * | 2016-01-31 | 2016-08-31 | 深圳市科恩环保有限公司 | Organic waste gas treatment system |
| US20170252693A1 (en) * | 2016-03-01 | 2017-09-07 | Seibu Giken Co., Ltd. | Absorption type removal / concentration apparatus |
| CN208032297U (en) * | 2018-02-01 | 2018-11-02 | 浙江大学 | A kind of fish meal production low exhaust emission device |
-
2018
- 2018-02-01 CN CN201810102552.1A patent/CN108295628A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101185820A (en) * | 2007-08-24 | 2008-05-28 | 陈昆柏 | Method and device for fathering fish powder waste gases |
| CN205516946U (en) * | 2016-01-31 | 2016-08-31 | 深圳市科恩环保有限公司 | Organic waste gas treatment system |
| US20170252693A1 (en) * | 2016-03-01 | 2017-09-07 | Seibu Giken Co., Ltd. | Absorption type removal / concentration apparatus |
| CN105698521A (en) * | 2016-03-30 | 2016-06-22 | 广东环葆嘉节能科技有限公司 | Hot-air drying system and method |
| CN208032297U (en) * | 2018-02-01 | 2018-11-02 | 浙江大学 | A kind of fish meal production low exhaust emission device |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109045932A (en) * | 2018-09-20 | 2018-12-21 | 岭商（浙江）生物科技有限公司 | A kind of exhaust treatment system and its treatment process of fish meal |
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Application publication date: 20180720 |
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