CN109824397A - A kind of reaction kettle with moisture separation device - Google Patents
A kind of reaction kettle with moisture separation device Download PDFInfo
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- CN109824397A CN109824397A CN201910163728.9A CN201910163728A CN109824397A CN 109824397 A CN109824397 A CN 109824397A CN 201910163728 A CN201910163728 A CN 201910163728A CN 109824397 A CN109824397 A CN 109824397A
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- reaction kettle
- air
- separation device
- moisture separation
- pipe
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 73
- 238000000926 separation method Methods 0.000 title claims abstract description 42
- 238000009833 condensation Methods 0.000 claims abstract description 34
- 230000005494 condensation Effects 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000005057 refrigeration Methods 0.000 claims abstract description 17
- 239000003507 refrigerant Substances 0.000 claims abstract description 14
- 238000001035 drying Methods 0.000 claims abstract description 7
- 239000007788 liquid Substances 0.000 claims description 42
- 239000002826 coolant Substances 0.000 claims description 38
- 238000001816 cooling Methods 0.000 claims description 36
- 239000006185 dispersion Substances 0.000 claims description 9
- 238000005192 partition Methods 0.000 claims description 9
- 239000000498 cooling water Substances 0.000 claims description 8
- 238000010943 off-gassing Methods 0.000 claims description 4
- 238000009423 ventilation Methods 0.000 claims description 3
- 230000001502 supplementing effect Effects 0.000 claims description 2
- 239000007789 gas Substances 0.000 abstract description 29
- 239000002912 waste gas Substances 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 10
- 230000007613 environmental effect Effects 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000000855 fermentation Methods 0.000 description 5
- 230000004151 fermentation Effects 0.000 description 5
- 239000003895 organic fertilizer Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000002994 raw material Substances 0.000 description 3
- 230000002745 absorbent Effects 0.000 description 2
- 239000002250 absorbent Substances 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 235000012054 meals Nutrition 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000010815 organic waste Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000012531 culture fluid Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
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- Drying Of Gases (AREA)
Abstract
The invention discloses a kind of reaction kettles with moisture separation device, including reaction kettle ontology, and the moisture separation device set on reaction kettle body exterior, exhaust system, air return system and refrigeration system；Moisture separation device is for the steam-water separation of reaction kettle exhaust and the condensation drying of separation gas；The exhaust gas generated in reaction kettle ontology is extracted out and is sent to moisture separation device by exhaust system, and dry gas is extracted out from moisture separation device and sent to reaction kettle ontology by air return system, and refrigeration system provides refrigerant for moisture separation device.Reaction kettle, moisture separation device, exhaust system and air return system constitute the circuit of a waste gas circulation, and reaction kettle exhaust recycles in a closed environment, drastically reduces reaction kettle capacity, reduce distributing for peculiar smell.
Description
Technical field
The present invention relates to environmental protection equipments, and in particular to a kind of for manufacturing the reaction kettle of organic fertilizer using organic waste as raw material
Equipment.
Background technique
Organic fertilizer production based on fermenting is usually with stalk, excrement and remaining meal rubbish etc. for raw material, when by one section
Between microbiological treatment, fermentation becomes qualified organic fertilizer.Reaction kettle as medium-sized processing equipment, have land occupation less, investment it is low,
The characteristics of flexible operation, the popularization and application suitable for organic fertilizer production.
Evaporation needs in fermentation process due to moisture content are exhausted, with organic wastes such as remaining meal rubbish, stalk, excrement
In the production process for making organic fertilizer for fermenting raw materials, due to the presence of fermentation, strong penetrating odor, ring are had in exhaust
Border is seriously polluted, therefore environmental issue limits the large-scale promotion of reaction kettle.
Summary of the invention
It is vented to solve existing reaction kettle by the way of outlet of uncapping, environmental pollution is serious, it is difficult to adapt to environmental protection
The technical issues of development, the present invention provide a kind of reaction kettle with moisture separation device, can make to generate in fermentation process
Steam carries out steam separation and condensation drying by the moisture separation device outside reaction kettle, then that gas after drying is again defeated
Enter reaction kettle, drastically reduce reaction kettle efflux gas, that is, reduces the steam outlet diffusion containing tangy, meet environmental protection
It is required that.
The first technical solution that the present invention uses is: a kind of reaction kettle with moisture separation device, including reaction kettle sheet
Body further includes moisture separation device, exhaust system, air return system and refrigeration system set on reaction kettle body exterior；Steam point
From device for the steam-water separation of reaction kettle exhaust and the condensation drying of separation gas；Exhaust system will generate in reaction kettle ontology
Exhaust gas extract out and send to moisture separation device, dry gas is extracted out from moisture separation device and is sent to reaction by air return system
Kettle ontology, refrigeration system provide refrigerant for moisture separation device.
The second technical solution that the present invention uses is the improvement in the first technical solution, the second technology that the present invention uses
Scheme is: the moisture separation device include one closing shell, housing cavity by be successively vertically arranged partition, split-wind plate one and
Split-wind plate two is isolated into the cooling chamber being sequentially connected to, separating chamber, condenses hothouse and out air compartment；The upside of partition is equipped with gas stream
Several exhaust vents are evenly equipped on circulation passage, split-wind plate one and split-wind plate two, cooling chamber is equipped with air inlet, and separating chamber is equipped with outlet
Mouthful.
The third technical solution that the present invention uses is the improvement in the second technical solution, the third technology that the present invention uses
Scheme is: being equipped with coolant liquid in the cooling chamber, is equipped with cooling coil and air inlet dispersion pipe, air inlet dispersion pipe one end in coolant liquid
In coolant liquid, the other end passes through air inlet and connect with exhaust system；Cooling coil is set to the bottom of coolant liquid, is passed through in pipe
Cooling water.
The 4th technical solution that the present invention uses is the improvement in third technical solution, the 4th technology that the present invention uses
Scheme is: the air inlet dispersion pipe includes the outlet branch of a general pipeline, a connecting tube and several horizontally disposed arranged in parallel
Pipe, one end of inlet manifold pass through air inlet and connect with exhaust system, and the other end is connected to by connecting tube with each going out gas branch pipe, often
The tube wall of a going out gas branch pipe is provided with several outgassing micropores, going out gas branch pipe endcapped.
The 5th technical solution that the present invention uses is the improvement in third technical solution, the 5th technology that the present invention uses
Scheme is: water inlet pipe, overflow pipe, the first temperature detecting resistance and the first drainpipe are additionally provided in the cooling chamber；Overflow pipe is for limiting
Coolant liquid is added for supplementing in the liquid level of coolant liquid processed, water inlet pipe, and the first temperature detecting resistance is used to measure the temperature of coolant liquid, and first
Drainpipe is set to the discharge that cooling chamber bottom is used for coolant liquid.
The 6th technical solution that the present invention uses is the improvement in the second technical solution, the 6th technology that the present invention uses
Scheme is: several condensation board groups is equipped at intervals in the condensation hothouse, the condensation board group is by spaced hollow condensation
Board group at, it is adjacent two condensation board group cold plates be staggered, hollow cold plate and condensation board group between by connecting tube connection,
Head end and the cold plate of end are respectively equipped with refrigerant inlet and refrigerant exit.
The 7th technical solution that the present invention uses is the improvement in the 6th technical solution, the 7th technology that the present invention uses
Scheme is: the one side towards separating chamber of the cold plate is equipped with fin, and fin one end end face is bonded company with cold plate side
It connects.
The 8th technical solution that the present invention uses is the improvement in the second technical solution, the 8th technology that the present invention uses
Scheme is: the second temperature detecting resistance and third temperature detecting resistance are respectively equipped in the separating chamber and out air compartment.
The 9th technical solution that the present invention uses is the improvement in the first technical solution, the 9th technology that the present invention uses
Scheme is: the exhaust system includes exhaust fan and air draft air hose, and exhaust fan is mounted on the left side of reaction kettle bodies top
On wall, fan inlet is connected to reaction kettle inner cavity, and fan outlet is connected to by air draft air hose with moisture separation device.
The tenth technical solution that the present invention uses is the improvement in the first technical solution, the tenth technology that the present invention uses
Scheme is: the air return system includes return air fan and return air air hose, and return air fan is mounted on the right side of reaction kettle bodies top
On wall, fan outlet is connected to reaction kettle inner cavity, and fan inlet is connected to by return air air hose with moisture separation device.
Beneficial effects of the present invention:
1, reaction kettle, moisture separation device, exhaust system and air return system constitute an exhaust recycle loop, reaction kettle
Exhaust recycles in a closed environment, drastically reduces reaction kettle capacity, reduces distributing for peculiar smell.
2, most of stink in reaction kettle exhaust is removed by coolant liquid condensed absorbent, the ingredient of coolant liquid can basis
Exhaust gas properties and the discharge index of environmental requirement reasonably select, flexible operation, good absorption effect, and use cost is controllable.
3, dry gas is back in reaction kettle, reduces the vapour quantity that reaction kettle further evaporates, and improves steam-water separation efficiency.
4, by coolant liquid condensed absorbent, the corrosive gas such as the hydrogen sulfide in exhaust gas can be removed, are reduced after secondary reuse
Corrosion to reaction kettle.
Detailed description of the invention
Fig. 1 is the schematic front view of the embodiment 1 of reaction kettle of the present invention with moisture separation device.
Fig. 2 is the top view of Fig. 1.
Specific embodiment
To make the object, technical solutions and advantages of the present invention clearer, below in conjunction with attached drawing and a kind of preferred reality
Mode is applied technical solution of the present invention is clearly and completely described.
In the following description, on the basis of the orientation of reaction kettle shown in Fig. 1, the top of reaction kettle as shown in the figure is
"upper", on the contrary it is "lower"；The left side of reaction kettle is " left side ", otherwise is " right side ".
Embodiment 1
Refering to fig. 1 and Fig. 2, the reaction kettle with moisture separation device include reaction kettle ontology 3, moisture separation device 8, row
Wind system, air return system and refrigerator system.In the present embodiment, reaction kettle ontology 3 is in horizontal setting.Exhaust system, return air
System, moisture separation device 8 and refrigerator system are set to the outside of reaction kettle ontology 3.
Moisture separation device 8 includes a closed shell, and housing cavity is by the partition 8-7, one 8-8 of split-wind plate that set gradually
And two 8-11 of split-wind plate is isolated into the cooling chamber 8-12 being sequentially connected to, separating chamber 8-13, condenses hothouse 8-14 and out air compartment 8-
16 4 parts.Partition 8-7, one 8-8 of split-wind plate and two 8-11 of split-wind plate are vertically arranged, and the upside of partition 8-7 is equipped with gas stream
Circulation passage.Several exhaust vents are evenly equipped on two 8-11 of one 8-8 of split-wind plate and split-wind plate, so that air-flow passes through.Split-wind plate one
8-8 plays the role of even distributing wind simultaneously.
Water inlet pipe 8-1, overflow pipe 8-2, the first temperature detecting resistance 8-3, air inlet dispersion pipe 8-4, cold is equipped in cooling chamber 8-12
But coil pipe 8-5, the first drainpipe 8-6 and coolant liquid.Coolant liquid can be taste removal bacteria culture fluid or water, according to reaction kettle when use
The property of exhaust gas and environmental requirement reasonably select.
Cooling coil 8-5 is set to the bottom of cooling chamber 8-12, horizontally disposed using back-shaped structure.It is continuous in cooling coil
It is passed through cooling water, gives coolant liquid cooling, cooling water originally pneumatics refrigeration system.Since recirculated cooling water and coolant liquid are complete by coil pipe
Full isolation, recirculated cooling water will not be contaminated, and reduce the generation of sewage.Air inlet dispersion pipe 8-4 is set to the top of cooling coil 8-5
And it is located at the lower part of cooling chamber, including a general pipeline, a connecting tube and several horizontally disposed going out gas branch pipe, air inlets side by side are total
One end of pipe is stretched out cooling chamber air inlet and is connect with exhaust system, and the other end is connected to by connecting tube with each going out gas branch pipe, each
The endcapped of going out gas branch pipe, tube wall offer several outgassing micropores.The measurement end of first temperature detecting resistance 8-3 protrudes into condensate liquid
For measuring the temperature of coolant liquid.Overflow pipe 8-2 is set to the middle and upper part of cooling chamber, for limiting the liquid level of coolant liquid.Water inlet pipe
8-1 is set to the top of cooling chamber, addition and supplement for coolant liquid.First drainpipe 8-6 is set to the bottom of cooling chamber, is used for
Coolant liquid is discharged.The outlet of first drainpipe 8-6 is arranged isolating valve, (not shown), and isolating valve, is closed when not drain.
Separating chamber 8-13 is a cavity, and left side is connected to by the air ventilation passage above partition 8-7 with cooling chamber 8-12,
Right side is connected to by the exhaust vent on one 8-8 of split-wind plate with condensation hothouse 8-14.The second thermometric electricity is equipped in separating chamber 8-13
8-18 is hindered, for measuring temperature in separating chamber 8-13.Cooling room temperature is higher, and it is lower to condense dry room temperature, and separating chamber can be with
It is effectively isolated cooling chamber and condensation chamber, the temperature transmitting of two Room is reduced, reduces influence of the cooling chamber to condensation room temperature, reduce system
The power consumption of cold.And one 8-8 of split-wind plate is also functioned to and is evenly distributed condensation hothouse into wind action, is conducive to improve condensation drying
Efficiency and effect.
Refrigeration system includes refrigeration machine 6 and refrigerant pipe 7.Refrigeration machine 6 is existing general refrigeration equipment, preferably single stage screw pressure
Contracting machine.
Several condensation board groups are equipped at intervals in condensation hothouse 8-14, every group of condensation board group includes several block gap settings
Hollow cold plate 8-10.Cold plate 8-10 is vertically arranged, and is fitted with several fins towards the side of separating chamber 8-13.Condensation
It is connected between plate 8-10 and condensation board group by connecting tube 8-15.The setting of fin is in order to enhance condensation effect.In the present embodiment
In, fin is a plate.In order to improve condensation effect, the cold plate in the cold plate of two groups of front and back is staggered, and condenses rear
The gap formed between two pieces of cold plates in front of plate face；Prevent air inlet without cold plate condensation i.e. from condensation hothouse 8-14
Discharge.Head end and the cold plate of end pass through refrigerant pipe 7 respectively and connect with refrigeration machine 6.Connecting tube 8-15, hollow cold plate 8-
10, refrigerant pipe 7 and refrigeration machine 6 form a circulating frozen system, the low temperature refrigerant come out from refrigeration machine 6 by refrigerant pipe 7 into
Enter connecting tube 8-15 and hollow cold plate 8-10, temperature after heat exchange is carried out in connecting tube 8-15 and hollow cold plate 8-10
It increases, high temperature refrigerant flows back to refrigeration machine 6 through refrigerant pipe 7 and cools down, and moves in circles.The bottom for condensing hothouse 8-14 is equipped with conical bottom
Plate, the center of bottom plate are connected with the outlet setting isolating valve, (not shown) of the second drainpipe 8-9, the second drainpipe 8-9.
Air compartment 8-16 is a cavity out, is connected by exhaust vent on two 8-11 of split-wind plate and the condensation hothouse 8-14 in left side
It is logical.Third temperature detecting resistance 8-19 is equipped in air compartment 8-16 out, for measuring temperature in air compartment 8-16.
Exhaust system includes exhaust fan 2 and air draft air hose 1, and exhaust fan 2 is mounted on the left side at 3 top of reaction kettle ontology
On wall, fan inlet is connected to reaction kettle inner cavity, and fan outlet is dispersed by the air inlet of air draft air hose 1 and moisture separation device 8
Pipe 8-4 connection.
Air return system includes return air fan 4 and return air air hose 5, and return air fan 4 is mounted on the right side at 3 top of reaction kettle ontology
On wall, fan outlet is connected to reaction kettle inner cavity, the air compartment 8- out that fan inlet passes through return air air hose 5 and moisture separation device 8
16 gas outlet connection.
Temperature detecting resistance is the prior art, selects the rod-type platinum resistance thermometer sensor, of general armouring in this application.
The working principle that the present invention will be described in detail for reaction kettle described in the embodiment 1 below is as follows:
The filling coolant liquid first in cooling chamber 8-12.First temperature detecting resistance 8-3 measures coolant temperature.
Material ferments in reaction kettle ontology 3, and a large amount of vapor generated in fermentation process are gathered in reaction kettle sheet
The saturation vapour of high temperature is formed at the top of body 3；
Exhaust fan 2 extracts saturation vapour in reaction kettle ontology 3 out, through air draft air hose 1 be delivered to cooling chamber 8-12 into
Gas dispersion pipe 8-4, and be dispersed in coolant liquid by the outgassing micropore in each going out gas branch pipe, it is cooling through the coolant liquid first step
And deodorization, most water vapour and stink are absorbed by coolant liquid；
Steam after cooled room 8-12 separation continues to rise, and enters separating chamber 8- through the gas passage on the upside of partition 8-7
13, the second temperature detecting resistance 8-18 measure temperature in separating chamber 8-13；
Gas in separating chamber 8-13 is stopped by one 8-8 of split-wind plate, through the exhaust vent on one 8-8 of split-wind plate even into cold
In solidifying room 8-14, and brush on first group of cold plate 8-10, steam condenses into water droplet to the cold, the non-condensing vapor in part after
It is continuous to move backward, it brushes and continues to condense into water droplet on spaced second group of cold plate, by the condensation point of each group cold plate
Decline from rear gas water capacity, gas enters air compartment 8-16, the water droplet of condensation through the exhaust vent of two 8-11 of split-wind plate after drying
It is collected in the second drainpipe 8-9 of condensation chamber bottom；
Third temperature detecting resistance 8-19 measures temperature in air compartment 8-16, and gas through outlet enters return air wind in air compartment 8-16 out
Pipe 5 is blasted in reaction kettle ontology 3 by return air fan 4 two times.
In order to keep the temperature of coolant liquid in cooling chamber in technology controlling and process range, when the first temperature detecting resistance 8-3 detect it is cold
But when liquid temperature is higher than temperature upper limit, cooling water amount in cooling coil 8-5 is increased, reduces coolant temperature；When temperature reduces
When to normal value, reduce cooling water amount, and maintained.Due to absorbing a large amount of steam in coolant liquid, liquid level is gradually
It increases, when reaching overflow pipe 8-2, is discharged through overflow pipe.Coolant liquid after a period of use, need replacing coolant liquid, beat
The first drainpipe 8-6 emptying coolant liquid is opened, and is supplemented by water inlet pipe 8-1.
In order to avoid a large amount of frostings on cold plate 8-10, ventilation is caused to be deteriorated, when detect the second temperature detecting resistance 8-18 with
The excessive temperature differentials of third temperature detecting resistance 8-19, and third temperature detecting resistance 8-19 temperature value it is relatively low when, reduce refrigeration machine 6 system
Cooling capacity, allows steam naturalization solution frosting；When the temperature difference for detecting the second temperature detecting resistance 8-18 and third temperature detecting resistance 8-19 is too small,
And when the temperature value of third temperature detecting resistance 8-19 is higher, increase the refrigerating capacity of refrigeration machine 6, guarantees condensation effect.
Not doing the part illustrated in above instructions is the prior art, or has both been able to achieve by the prior art.
Claims (10)
1. a kind of reaction kettle with moisture separation device, including reaction kettle ontology, which is characterized in that further include being set to reaction kettle
Moisture separation device, exhaust system, air return system and the refrigeration system of body exterior；Moisture separation device is vented for reaction kettle
Steam-water separation and separate gas condensation drying；The exhaust gas generated in reaction kettle ontology is extracted out and is sent to steam by exhaust system
Dry gas is extracted out from moisture separation device and is sent to reaction kettle ontology by separator, air return system, and refrigeration system is water
Steum separating device provides refrigerant.
2. reaction kettle as described in claim 1, which is characterized in that the moisture separation device includes a closing shell, shell
Inner cavity is isolated into the cooling chamber being sequentially connected to, separating chamber, condensation by the partition, split-wind plate one and split-wind plate two being successively vertically arranged
Hothouse and out air compartment；The upside of partition is equipped with air ventilation passage, is evenly equipped with several outlet air on split-wind plate one and split-wind plate two
Hole, cooling chamber are equipped with air inlet, and separating chamber is equipped with gas outlet.
3. reaction kettle as claimed in claim 2, which is characterized in that be equipped with coolant liquid in the cooling chamber, be equipped in coolant liquid
Cooling coil and air inlet dispersion pipe, air inlet dispersion pipe one end are set in coolant liquid, and the other end passes through air inlet and exhaust system connects
It connects；Cooling coil is set to the bottom of coolant liquid, is passed through cooling water in pipe.
4. reaction kettle as claimed in claim 3, which is characterized in that the air inlet dispersion pipe includes a general pipeline, a connection
The going out gas branch pipe of pipe and several horizontally disposed arranged in parallel, one end of inlet manifold pass through air inlet and connect with exhaust system,
The other end is connected to by connecting tube with each going out gas branch pipe, and the tube wall of each going out gas branch pipe is provided with several outgassing micropores, outlet branch
Pipe end closing.
5. reaction kettle as claimed in claim 3, which is characterized in that be additionally provided with water inlet pipe, overflow pipe, first in the cooling chamber
Temperature detecting resistance and the first drainpipe；Overflow pipe is used to limit the liquid level of coolant liquid, and coolant liquid is added for supplementing in water inlet pipe, and first
Temperature detecting resistance is used to measure the temperature of coolant liquid, and the first drainpipe is set to the discharge that cooling chamber bottom is used for coolant liquid.
6. reaction kettle as claimed in claim 2, which is characterized in that be equipped at intervals with several cold plates in the condensation hothouse
Group, the condensation board group are made of spaced hollow cold plate, and the cold plate of adjacent two condensations board group is staggered, hollow
It is connected between cold plate and condensation board group by connecting tube, the cold plate of head end and end is respectively equipped with refrigerant inlet and refrigerant goes out
Mouthful.
7. reaction kettle as claimed in claim 6, which is characterized in that the one side towards separating chamber of the cold plate is equipped with wing
Piece, fin one end end face are fitted and connected with cold plate side.
8. reaction kettle as claimed in claim 2, which is characterized in that be respectively equipped with the second thermometric in the separating chamber and out air compartment
Resistance and third temperature detecting resistance.
9. reaction kettle as described in claim 1, which is characterized in that the exhaust system includes exhaust fan and air draft air hose,
Exhaust fan is mounted on the left side wall of reaction kettle bodies top, and fan inlet is connected to reaction kettle inner cavity, and fan outlet passes through
Air draft air hose is connected to moisture separation device.
10. reaction kettle as described in claim 1, which is characterized in that the air return system includes return air fan and return air air hose,
Return air fan is mounted on the right side wall of reaction kettle bodies top, and fan outlet is connected to reaction kettle inner cavity, and fan inlet passes through
Return air air hose is connected to moisture separation device.
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| CN201910163728.9A CN109824397A (en) | 2019-03-05 | 2019-03-05 | A kind of reaction kettle with moisture separation device |
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| CN201910163728.9A CN109824397A (en) | 2019-03-05 | 2019-03-05 | A kind of reaction kettle with moisture separation device |
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