CN209974651U - Reation kettle with steam separator - Google Patents
Reation kettle with steam separator Download PDFInfo
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- CN209974651U CN209974651U CN201920277678.2U CN201920277678U CN209974651U CN 209974651 U CN209974651 U CN 209974651U CN 201920277678 U CN201920277678 U CN 201920277678U CN 209974651 U CN209974651 U CN 209974651U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 70
- 238000006243 chemical reaction Methods 0.000 claims abstract description 50
- 239000007789 gas Substances 0.000 claims abstract description 30
- 238000000926 separation method Methods 0.000 claims abstract description 30
- 238000009833 condensation Methods 0.000 claims abstract description 24
- 230000005494 condensation Effects 0.000 claims abstract description 24
- 238000001035 drying Methods 0.000 claims abstract description 18
- 239000003507 refrigerant Substances 0.000 claims abstract description 14
- 239000002912 waste gas Substances 0.000 claims abstract description 7
- 239000000110 cooling liquid Substances 0.000 claims description 40
- 238000001816 cooling Methods 0.000 claims description 37
- 239000006185 dispersion Substances 0.000 claims description 12
- 239000000498 cooling water Substances 0.000 claims description 8
- 238000005192 partition Methods 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 5
- 238000005057 refrigeration Methods 0.000 claims description 5
- 238000007599 discharging Methods 0.000 claims description 3
- 230000001502 supplementing effect Effects 0.000 claims description 3
- 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
- 239000002994 raw material Substances 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000010813 municipal solid waste Substances 0.000 description 3
- 239000003895 organic fertilizer Substances 0.000 description 3
- 238000003912 environmental pollution Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000010902 straw Substances 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
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- -1 excrement Substances 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
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- Drying Of Gases (AREA)
Abstract
The utility model discloses a reaction kettle with a water-vapor separation device, which comprises a reaction kettle body, and the water-vapor separation device, an exhaust system, a return air system and a refrigerating system which are arranged outside the reaction kettle body; the water-vapor separation device is used for steam-water separation of the exhaust gas of the reaction kettle and condensation drying of the separated gas; exhaust system takes out the waste gas that produces in with the reation kettle body and sends to water vapor separator, and air return system takes out dry gas from water vapor separator and sends to the reation kettle body, and refrigerating system provides the refrigerant for water vapor separator. The reaction kettle, the water-vapor separation device, the exhaust system and the air return system form a loop of waste gas circulation, exhaust of the reaction kettle circulates in a closed environment, the exhaust amount of the reaction kettle is greatly reduced, and emission of peculiar smell is reduced.
Description
Technical Field
The utility model relates to an environmental protection equipment, concretely relates to a reation kettle equipment that is used for using organic rubbish to make fertilizer as the raw materials.
Background
The organic fertilizer production mainly by fermentation usually takes straws, excrement, food wastes and the like as raw materials, and the raw materials are fermented into qualified organic fertilizers after a period of microbial treatment. The reaction kettle is used as a medium-sized processing device, has the characteristics of small occupied area, low investment and flexible operation, and is suitable for popularization and application of organic fertilizer production.
In the fermentation process, because the evaporation of water needs to be exhausted, in the production process of preparing the organic fertilizer by fermenting the organic garbage such as the food garbage, the straws, the excrement and the like as raw materials, the exhaust gas has strong pungent smell due to the existence of fermentation, and the environmental pollution is serious, so the environmental protection problem limits the large-scale popularization of the reaction kettle.
SUMMERY OF THE UTILITY MODEL
In order to solve current reation kettle and adopt the mode exhaust of uncapping outer row, environmental pollution is serious, is difficult to adapt to the technical problem of the development of environmental protection, the utility model provides a reation kettle with steam separator can make the steam that produces among the fermentation process carry out steam separation and condensation drying through the outside steam separator of reation kettle, then with gaseous reentrant reation kettle in the drying back, has reduced the outer exhaust gas of reation kettle by a wide margin, reduces the outer diffusion of arranging of steam that contains strong smell promptly, satisfies the environmental protection requirement.
The utility model discloses a first technical scheme be: a reaction kettle with a water-vapor separation device comprises a reaction kettle body, and further comprises the water-vapor separation device, an exhaust system, an air return system and a refrigeration system which are arranged outside the reaction kettle body; the water-vapor separation device is used for steam-water separation of the exhaust gas of the reaction kettle and condensation drying of the separated gas; exhaust system takes out the waste gas that produces in with the reation kettle body and sends to water vapor separator, and air return system takes out dry gas from water vapor separator and sends to the reation kettle body, and refrigerating system provides the refrigerant for water vapor separator.
The utility model discloses a second technical scheme be the improvement on first technical scheme, the utility model discloses a second technical scheme be: the water-vapor separation device comprises a closed shell, and an inner cavity of the shell is partitioned into a cooling chamber, an air distribution chamber, a condensation drying chamber and an air outlet chamber which are sequentially communicated by a partition plate, an air distribution plate I and an air distribution plate II which are sequentially and vertically arranged; the upper side of the partition plate is provided with a gas circulation channel, the first air distribution plate and the second air distribution plate are uniformly provided with a plurality of air outlet holes, the cooling chamber is provided with an air inlet, and the air distribution chamber is provided with an air outlet.
The utility model discloses a third technical scheme be the improvement on the second technical scheme, the utility model discloses a third technical scheme be: the cooling chamber is internally provided with cooling liquid, the cooling liquid is internally provided with a cooling coil and an air inlet dispersion pipe, one end of the air inlet dispersion pipe is arranged in the cooling liquid, and the other end of the air inlet dispersion pipe penetrates through the air inlet to be connected with an exhaust system; the cooling coil is arranged at the bottom of the cooling liquid, and cooling water is introduced into the cooling coil.
The utility model discloses a fourth technical scheme be the improvement on the third technical scheme, the utility model discloses a fourth technical scheme be: the air inlet dispersion pipe comprises a main pipe, a connecting pipe and a plurality of air outlet branch pipes which are horizontally arranged and arranged in parallel, one end of the air inlet main pipe penetrates through the air inlet to be connected with the exhaust system, the other end of the air inlet main pipe is communicated with the air outlet branch pipes through the connecting pipe, a plurality of air outlet micropores are formed in the pipe wall of each air outlet branch pipe, and the tail ends of the air outlet branch pipes are sealed.
The utility model discloses a fifth technical scheme be the improvement on the third technical scheme, the utility model discloses a fifth technical scheme be: the cooling chamber is also internally provided with a water inlet pipe, an overflow pipe, a first temperature measuring resistor and a first water drainage pipe; the overflow pipe is used for limiting the liquid level of the cooling liquid, the water inlet pipe is used for supplementing and adding the cooling liquid, the first temperature measuring resistor is used for measuring the temperature of the cooling liquid, and the first water discharge pipe is arranged at the bottom of the cooling chamber and used for discharging the cooling liquid.
The utility model discloses a sixth technical scheme be the improvement on the second technical scheme, the utility model discloses a sixth technical scheme be: the condensing and drying chamber is internally provided with a plurality of condensing plate groups at intervals, each condensing plate group consists of hollow condensing plates arranged at intervals, the condensing plates of two adjacent condensing plate groups are arranged in a staggered manner, the hollow condensing plates and the condensing plate groups are communicated through connecting pipes, and the condensing plates at the head end and the tail end are respectively provided with a refrigerant inlet and a refrigerant outlet.
The utility model discloses a seventh technical scheme be the improvement on the sixth technical scheme, the utility model discloses a seventh technical scheme be: and fins are arranged on one side surface of the condensing plate facing the air distribution chamber, and the end surface of one end of each fin is in fit connection with the side surface of the condensing plate.
The utility model discloses an eighth technical scheme be the improvement on the second technical scheme, the utility model discloses an eighth technical scheme be: and a second temperature measuring resistor and a third temperature measuring resistor are respectively arranged in the air dividing chamber and the air outlet chamber.
The utility model discloses a ninth technical scheme be the improvement on first technical scheme, the utility model discloses a ninth technical scheme be: the exhaust system comprises an exhaust fan and an exhaust air pipe, the exhaust fan is installed on the left side wall of the top of the reaction kettle body, an inlet of the fan is communicated with the inner cavity of the reaction kettle, and an outlet of the fan is communicated with the water-vapor separation device through the exhaust air pipe.
The utility model discloses a tenth technical scheme be the improvement on first technical scheme, the utility model discloses a tenth technical scheme be: the air return system comprises an air return fan and an air return air pipe, the air return fan is installed on the right side wall of the top of the reaction kettle body, the outlet of the fan is communicated with the inner cavity of the reaction kettle, and the inlet of the fan is communicated with the water-vapor separation device through the air return air pipe.
The utility model has the advantages that:
1. the reaction kettle, the water-vapor separation device, the exhaust system and the air return system form a waste gas circulation loop, exhaust of the reaction kettle circulates in a closed environment, the exhaust amount of the reaction kettle is greatly reduced, and emission of peculiar smell is reduced.
2. Most of odor in the exhaust of the reaction kettle is removed through cooling liquid condensation and absorption, the components of the cooling liquid can be reasonably selected according to the exhaust gas properties and the emission indexes of environmental protection requirements, the operation is flexible, the absorption effect is good, and the use cost is controllable.
3. And the dry gas returns to the reaction kettle, so that the further evaporation water vapor amount of the reaction kettle is reduced, and the steam-water separation efficiency is improved.
4. Through cooling liquid condensation and absorption, corrosive gases such as hydrogen sulfide in waste gas can be removed, and corrosion to the reaction kettle is reduced after secondary recycling.
Drawings
Fig. 1 is a schematic front view of embodiment 1 of the reaction kettle with a water-vapor separation device of the present invention.
Fig. 2 is a top view of fig. 1.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention clearer, the technical solutions of the present invention will be clearly and completely described below with reference to the accompanying drawings and a preferred embodiment.
In the following description, the upper side of the reaction vessel shown in fig. 1 is referred to as "upper" and the opposite side is referred to as "lower" based on the orientation of the reaction vessel; the left side of the reaction kettle is the left side, and the opposite is the right side.
Embodiment mode 1
Referring to fig. 1 and 2, the reaction kettle with the water-vapor separation device includes a reaction kettle body 3, a water-vapor separation device 8, an exhaust system, an air return system, and a refrigerator system. In this embodiment, the reaction vessel body 3 is horizontally disposed. The exhaust system, the return air system, the water-vapor separation device 8 and the refrigerator system are arranged outside the reaction kettle body 3.
The water-vapor separation device 8 comprises a closed shell, and the inner cavity of the shell is partitioned into four parts, namely a cooling chamber 8-12, an air dividing chamber 8-13, a condensation drying chamber 8-14 and an air outlet chamber 8-16 which are communicated in sequence by a partition plate 8-7, an air dividing plate I8-8 and an air dividing plate II 8-11 which are arranged in sequence. The partition plate 8-7, the first air distribution plate 8-8 and the second air distribution plate 8-11 are vertically arranged, and the upper side of the partition plate 8-7 is provided with an air circulation channel. A plurality of air outlet holes are uniformly distributed on the first air distribution plate 8-8 and the second air distribution plate 8-11 so as to lead the air flow to pass smoothly. The first air distribution plate 8-8 simultaneously has the function of uniformly distributing air.
The cooling chamber 8-12 is internally provided with a water inlet pipe 8-1, an overflow pipe 8-2, a first temperature measuring resistor 8-3, an air inlet dispersion pipe 8-4, a cooling coil pipe 8-5, a first water discharge pipe 8-6 and cooling liquid. The cooling liquid can be odor removing bacteria culture solution or water, and is reasonably selected according to the nature of the waste gas of the reaction kettle and the environmental protection requirement when in use.
The cooling coil 8-5 is arranged at the bottom of the cooling chamber 8-12, adopts a clip structure and is horizontally arranged. And cooling water is continuously introduced into the cooling coil to cool the cooling liquid, and the cooling water is supplied to the air compression refrigeration system. Because the circulating cooling water and the cooling liquid are completely isolated by the coil, the circulating cooling water is not polluted, and the generation of sewage is reduced. The air inlet dispersion pipe 8-4 is arranged above the cooling coil pipe 8-5 and is positioned at the lower part of the cooling chamber and comprises a main pipe, a connecting pipe and a plurality of air outlet branch pipes which are horizontally arranged in parallel, one end of the air inlet main pipe extends out of an air inlet of the cooling chamber to be connected with an exhaust system, the other end of the air inlet main pipe is communicated with the air outlet branch pipes through the connecting pipe, the tail end of each air outlet branch pipe is sealed, and a plurality of air outlet micropores are formed in the. The measuring end of the first temperature measuring resistor 8-3 extends into the condensate for measuring the temperature of the cooling liquid. An overflow pipe 8-2 is provided in the middle upper part of the cooling chamber for limiting the level of the cooling liquid. The water inlet pipe 8-1 is arranged at the top of the cooling chamber and is used for adding and supplementing cooling liquid. The first drain pipe 8-6 is provided at the bottom of the cooling chamber for discharging the cooling liquid. The outlet of the first drain pipe 8-6 is provided with a blocking valve (not shown in the figure), which is closed when no liquid is drained.
The air dividing chamber 8-13 is a cavity, the left side is communicated with the cooling chamber 8-12 through a gas circulation channel above the partition plate 8-7, and the right side is communicated with the condensing and drying chamber 8-14 through an air outlet hole on the air dividing plate I8-8. A second temperature measuring resistor 8-18 is arranged in the air dividing chamber 8-13 and is used for measuring the temperature in the air dividing chamber 8-13. The cooling chamber has higher temperature, the condensation drying chamber has lower temperature, and the air dividing chamber can effectively isolate the cooling chamber from the condensing chamber, thereby reducing the temperature transmission of the two chambers, reducing the influence of the cooling chamber on the temperature of the condensing chamber and reducing the power consumption of the refrigerator. And the first air distribution plate 8-8 also plays a role in uniformly distributing the inlet air of the condensation drying chamber, thereby being beneficial to improving the efficiency and the effect of condensation drying.
The refrigerating system includes a refrigerator 6 and a refrigerant pipe 7. The refrigerator 6 is an existing general refrigeration device, preferably a single-stage screw compressor.
A plurality of condensing plate groups are arranged in the condensing and drying chambers 8-14 at intervals, and each condensing plate group comprises a plurality of hollow condensing plates 8-10 arranged at intervals. The condensing plate 8-10 is vertically arranged, and a plurality of fins are attached to the side surface facing the air separating chamber 8-13. The condensing plates 8-10 are communicated with the condensing plate groups through connecting pipes 8-15. The fins are arranged to enhance the condensation effect. In the present embodiment, the fin is a flat plate. In order to improve the condensation effect, the condensation plates in the front and rear two groups of condensation plates are staggered, so that the rear condensation plate is right opposite to the gap formed between the front two condensation plates; the inlet air is prevented from being discharged from the condensation drying chambers 8-14 without being condensed by the condensing plates. The condensation plates at the head end and the tail end are respectively connected with a refrigerator 6 through refrigerant pipes 7. The connecting pipes 8-15, the hollow condensing plates 8-10, the refrigerant pipe 7 and the refrigerator 6 form a circulating refrigeration system, low-temperature refrigerant from the refrigerator 6 enters the connecting pipes 8-15 and the hollow condensing plates 8-10 through the refrigerant pipe 7, the temperature is increased after heat exchange is carried out in the connecting pipes 8-15 and the hollow condensing plates 8-10, and high-temperature refrigerant flows back to the refrigerator 6 through the refrigerant pipe 7 to be cooled and circulates repeatedly. The bottom of the condensation drying chamber 8-14 is provided with a conical bottom plate, the center of the bottom plate is connected with a second water discharge pipe 8-9, and the outlet of the second water discharge pipe 8-9 is provided with a closing valve (not shown in the figure).
The air outlet chamber 8-16 is a cavity and is communicated with the left condensation drying chamber 8-14 through an air outlet hole on the second air distribution plate 8-11. A third temperature measuring resistor 8-19 is arranged in the air outlet chamber 8-16 and is used for measuring the temperature in the air outlet chamber 8-16.
The exhaust system comprises an exhaust fan 2 and an exhaust air pipe 1, the exhaust fan 2 is installed on the left side wall of the top of the reaction kettle body 3, the inlet of the fan is communicated with the inner cavity of the reaction kettle, and the outlet of the fan is communicated with an air inlet dispersion pipe 8-4 of the water-vapor separation device 8 through the exhaust air pipe 1.
The air return system comprises an air return fan 4 and an air return air pipe 5, the air return fan 4 is installed on the right side wall of the top of the reaction kettle body 3, the outlet of the fan is communicated with the inner cavity of the reaction kettle, and the inlet of the fan is communicated with the air outlets of the air outlet chambers 8-16 of the water-vapor separation device 8 through the air return air pipe 5.
The temperature measuring resistor is the prior art, and a general armored rod type platinum thermal resistor is selected in the application.
The following will explain the working principle of the present invention in detail by taking the reaction kettle described in embodiment 1 as an example:
the cooling chambers 8-12 are first filled with cooling liquid. The first temperature measuring resistor 8-3 measures the temperature of the cooling liquid.
The materials are fermented in the reaction kettle body 3, and a large amount of water vapor generated in the fermentation process is gathered at the upper part of the reaction kettle body 3 to form high-temperature saturated water vapor;
the exhaust fan 2 extracts saturated water vapor in the reaction kettle body 3, the saturated water vapor is conveyed to an air inlet dispersion pipe 8-4 of a cooling chamber 8-12 through an exhaust air pipe 1 and is uniformly dispersed in cooling liquid through air outlet micropores on each air outlet branch pipe, the saturated water vapor is cooled and deodorized through the cooling liquid for the first step, and most of the water vapor and odor are absorbed by the cooling liquid;
the water vapor separated by the cooling chamber 8-12 continuously rises and enters the air separating chamber 8-13 through the gas channel at the upper side of the clapboard 8-7, and the second temperature measuring resistor 8-18 measures the temperature in the air separating chamber 8-13;
the gas in the air dividing chamber 8-13 is blocked by the first air dividing plate 8-8, uniformly enters the condensing chamber 8-14 through the air outlet holes on the first air dividing plate 8-8, is blown onto the first group of condensing plates 8-10, water vapor is condensed into water drops when meeting with condensation, part of uncondensed water vapor continues to move backwards, is blown onto the second group of condensing plates arranged at intervals and continues to be condensed into water drops, the moisture content of the gas is reduced after condensation and separation of the groups of condensing plates, the dried gas enters the air outlet chamber 8-16 through the air outlet holes of the second air dividing plate 8-11, and the condensed water drops are collected into the second water outlet pipe 8-9 at the bottom of the condensing chamber;
the third temperature measuring resistor 8-19 measures the temperature in the air chamber 8-16, the air in the air outlet chamber 8-16 enters the air return pipe 5 through the outlet, and is blown into the reaction kettle body 3 by the air return fan 4 for the second time.
In order to keep the temperature of the cooling liquid in the cooling chamber within the process control range, when the first temperature measuring resistor 8-3 detects that the temperature of the cooling liquid is higher than the upper temperature limit, the cooling water consumption in the cooling coil 8-5 is increased, and the temperature of the cooling liquid is reduced; when the temperature is reduced to a normal value, the amount of cooling water is reduced and maintained. Since the cooling liquid absorbs a large amount of water vapor, the liquid level rises gradually, and when reaching the overflow pipe 8-2, the liquid is discharged through the overflow pipe. After the cooling liquid is used for a period of time, the cooling liquid needs to be replaced, the first water outlet pipe 8-6 is opened to empty the cooling liquid, and the cooling liquid is supplemented through the water inlet pipe 8-1.
In order to avoid frosting on the condensing plate 8-10 in a large amount and poor ventilation, when the temperature difference between the second temperature measuring resistor 8-18 and the third temperature measuring resistor 8-19 is detected to be overlarge and the temperature value of the third temperature measuring resistor 8-19 is detected to be low, the refrigerating capacity of the refrigerating machine 6 is reduced, and water vapor is naturally defrosted; when the temperature difference between the second temperature measuring resistor 8-18 and the third temperature measuring resistor 8-19 is detected to be too small and the temperature value of the third temperature measuring resistor 8-19 is detected to be too high, the refrigerating capacity of the refrigerating machine 6 is increased, and the condensing effect is ensured.
Parts which are not specifically described in the above description are prior art or can be realized by the prior art.
Claims (10)
1. A reaction kettle with a water-vapor separation device comprises a reaction kettle body, and is characterized by also comprising the water-vapor separation device, an exhaust system, an air return system and a refrigeration system which are arranged outside the reaction kettle body; the water-vapor separation device is used for steam-water separation of the exhaust gas of the reaction kettle and condensation drying of the separated gas; exhaust system takes out the waste gas that produces in with the reation kettle body and sends to water vapor separator, and air return system takes out dry gas from water vapor separator and sends to the reation kettle body, and refrigerating system provides the refrigerant for water vapor separator.
2. The reaction kettle according to claim 1, wherein the water-vapor separation device comprises a closed shell, and an inner cavity of the shell is partitioned into a cooling chamber, an air dividing chamber, a condensation drying chamber and an air outlet chamber which are sequentially communicated by a partition plate, an air dividing plate I and an air dividing plate II which are vertically arranged in sequence; the upper side of the partition plate is provided with a gas circulation channel, the first air distribution plate and the second air distribution plate are uniformly provided with a plurality of air outlet holes, the cooling chamber is provided with an air inlet, and the air distribution chamber is provided with an air outlet.
3. The reactor according to claim 2, wherein the cooling chamber is filled with a cooling liquid, the cooling liquid is filled with a cooling coil and an air inlet dispersion pipe, one end of the air inlet dispersion pipe is arranged in the cooling liquid, and the other end of the air inlet dispersion pipe passes through the air inlet and is connected with an exhaust system; the cooling coil is arranged at the bottom of the cooling liquid, and cooling water is introduced into the cooling coil.
4. The reactor according to claim 3, wherein the gas inlet dispersion pipe comprises a main pipe, a connecting pipe and a plurality of horizontally arranged gas outlet branch pipes arranged in parallel, one end of the gas inlet main pipe passes through the gas inlet and is connected with the exhaust system, the other end of the gas inlet main pipe is communicated with each gas outlet branch pipe through the connecting pipe, the pipe wall of each gas outlet branch pipe is provided with a plurality of gas outlet micropores, and the tail ends of the gas outlet branch pipes are closed.
5. The reactor according to claim 3, wherein the cooling chamber is further provided with a water inlet pipe, an overflow pipe, a first temperature measuring resistor and a first water discharge pipe; the overflow pipe is used for limiting the liquid level of the cooling liquid, the water inlet pipe is used for supplementing and adding the cooling liquid, the first temperature measuring resistor is used for measuring the temperature of the cooling liquid, and the first water discharge pipe is arranged at the bottom of the cooling chamber and used for discharging the cooling liquid.
6. The reactor of claim 2, wherein the condensing and drying chamber is partitioned into a plurality of condensing plate groups, each condensing plate group comprises hollow condensing plates spaced apart from each other, the condensing plates of two adjacent condensing plate groups are staggered, the hollow condensing plates and the condensing plate groups are communicated with each other through connecting pipes, and the condensing plates at the front end and the tail end are respectively provided with a refrigerant inlet and a refrigerant outlet.
7. The reactor of claim 6, wherein the side of the condensing plate facing the air dividing chamber is provided with a fin, and one end face of the fin is in fit connection with the side of the condensing plate.
8. The reactor of claim 2, wherein the air dividing chamber and the air outlet chamber are respectively provided with a second temperature measuring resistor and a third temperature measuring resistor.
9. The reactor of claim 1, wherein the exhaust system comprises an exhaust fan and an exhaust duct, the exhaust fan is mounted on the left side wall of the top of the reactor body, the inlet of the fan is communicated with the inner cavity of the reactor, and the outlet of the fan is communicated with the water-vapor separation device through the exhaust duct.
10. The reaction kettle according to claim 1, wherein the air return system comprises an air return fan and an air return pipe, the air return fan is arranged on the right side wall of the top of the reaction kettle body, the outlet of the fan is communicated with the inner cavity of the reaction kettle, and the inlet of the fan is communicated with the water-vapor separation device through the air return pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920277678.2U CN209974651U (en) | 2019-03-05 | 2019-03-05 | Reation kettle with steam separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920277678.2U CN209974651U (en) | 2019-03-05 | 2019-03-05 | Reation kettle with steam separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209974651U true CN209974651U (en) | 2020-01-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920277678.2U Expired - Fee Related CN209974651U (en) | 2019-03-05 | 2019-03-05 | Reation kettle with steam separator |
Country Status (1)
| Country | Link |
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| CN (1) | CN209974651U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109824397A (en) * | 2019-03-05 | 2019-05-31 | 南京西普环保科技有限公司 | A kind of reaction kettle with moisture separation device |
-
2019
- 2019-03-05 CN CN201920277678.2U patent/CN209974651U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109824397A (en) * | 2019-03-05 | 2019-05-31 | 南京西普环保科技有限公司 | A kind of reaction kettle with moisture separation device |
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