CN110844909A - Silicon dioxide hydrolysis furnace for producing rubber and plastic sealing elements - Google Patents
Silicon dioxide hydrolysis furnace for producing rubber and plastic sealing elements Download PDFInfo
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- CN110844909A CN110844909A CN201911156308.4A CN201911156308A CN110844909A CN 110844909 A CN110844909 A CN 110844909A CN 201911156308 A CN201911156308 A CN 201911156308A CN 110844909 A CN110844909 A CN 110844909A
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- pipe
- air
- hydrolysis furnace
- furnace body
- hydrolysis
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D17/00—Arrangements for circulating cooling fluids; Arrangements for circulating gas, e.g. air, within refrigerated spaces
- F25D17/04—Arrangements for circulating cooling fluids; Arrangements for circulating gas, e.g. air, within refrigerated spaces for circulating air, e.g. by convection
- F25D17/06—Arrangements for circulating cooling fluids; Arrangements for circulating gas, e.g. air, within refrigerated spaces for circulating air, e.g. by convection by forced circulation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D9/00—Cooling of furnaces or of charges therein
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D9/00—Cooling of furnaces or of charges therein
- F27D2009/007—Cooling of charges therein
- F27D2009/0072—Cooling of charges therein the cooling medium being a gas
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Inorganic Chemistry (AREA)
- Silicon Compounds (AREA)
Abstract
The invention relates to the technical field of silicon dioxide hydrolysis furnaces, and discloses a silicon dioxide hydrolysis furnace for producing rubber and plastic sealing elements. According to the invention, the air cooler is started, so that the air cooler conveys cold air into the cooling chamber through the air cooler exhaust pipeline, the blower absorbs the cold air, the cold air enters the hydrolysis furnace body from the air inlet pipe along the air outlet pipe to cool silica in the cooling chamber, then the air with heat is filtered by the filter screen and enters the cooling chamber along the circulating pipe to be cooled again, and then the blower conveys the air after being cooled again into the hydrolysis furnace body from the air inlet pipe along the air outlet pipe to be cooled, so that the air with high heat can not be directly discharged into the air, the environment is not polluted by heat energy, the air can be recycled, and the practicability of the device is increased.
Description
Technical Field
The invention relates to the technical field of silicon dioxide hydrolysis furnaces, in particular to a silicon dioxide hydrolysis furnace for producing rubber and plastic sealing elements.
Background
The silica hydrolysis furnace is one of the most important facilities in a silica production plant. The aerosol after the reaction from the nozzle enters the hydrolysis furnace from top to bottom under the action of negative pressure, exchanges heat with air serving as a cooling medium in the furnace body, and then flows out from a discharge hole at the bottom of the furnace body, so that the temperature of the aerosol can be reduced to meet the process requirements of subsequent processes.
The hydrolysis furnace in the prior art is not reasonable enough in structural configuration, high-temperature silicon dioxide aerosol only flows through for a short time in the hydrolysis furnace, and then directly pours to the bottom of the hydrolysis furnace and flows out, the structure of the heat exchange has the defect of small heat exchange area in the furnace body, the high-temperature silicon dioxide aerosol can not be integrally cooled to the required temperature, the normal operation of the next procedure can be seriously influenced, cooling gas after the heat exchange is generally directly discharged to air, the air containing high heat is directly discharged to the air, heat energy pollution can be caused to the environment, and cyclic utilization can not be carried out, so that the silicon dioxide hydrolysis furnace for producing the rubber and plastic sealing element is provided.
Disclosure of Invention
The invention aims to provide a silicon dioxide hydrolysis furnace for producing rubber and plastic sealing elements, which can achieve the purpose of recycling cooling gas.
In order to achieve the purpose, the invention provides the following technical scheme: a silica hydrolysis furnace for rubber and plastic sealing element production comprises a hydrolysis furnace body, wherein the left side and the right side of the bottom of the hydrolysis furnace body are fixedly connected with supporting plates, the bottom of each supporting plate is provided with a bottom plate, the two supporting plates are positioned on the two sides of the bottom plate and are respectively fixedly connected with the bottom plate, the four corners of the bottom plate are fixedly connected with supporting legs, the bottoms of the four supporting legs are respectively fixedly connected with a fixed seat, the top of the hydrolysis furnace body is provided with an inlet pipe, the inlet pipe penetrates through the hydrolysis furnace body and extends into the hydrolysis furnace body, the inside of the hydrolysis furnace body is provided with a cooling pipe, one end of the inlet pipe penetrating into the hydrolysis furnace body is connected with the cooling pipe, the lower right corner of the bottom of the hydrolysis furnace body is provided with a discharging pipe, one end, the end, far away from the feeding pipe, of the cooling pipe is connected with the discharging pipe, the end, far away from the hydrolysis furnace body, of the discharging pipe penetrates through the bottom plate and extends to the outside of the bottom plate, the upper right corner of the hydrolysis furnace body is provided with an air inlet pipe, the air inlet pipe penetrates through the hydrolysis furnace body and extends to the inside of the hydrolysis furnace body, one end, close to the air inlet pipe, of the hydrolysis furnace body is provided with a first fixing plate, the first fixing plate is fixedly connected with the hydrolysis furnace body, the top of the first fixing plate is fixedly connected with a blower, the output end of the blower is fixedly connected with an air outlet pipe, one end, far away from the blower, of the air outlet pipe is connected with the air inlet pipe, the left lower end of the hydrolysis furnace body is provided with an air outlet pipe, the bottom of fixed plate one is provided with fixed plate two, fixed plate two and hydrolysis furnace body fixed connection, two top fixedly connected with cooling chambers of fixed plate, the one end that the outlet duct was kept away from to the circulating pipe runs through fixed plate two and communicates with the cooling chamber, the cooling chamber top is provided with the connecting pipe, the one end and the cooling chamber intercommunication that the connecting pipe is close to the cooling chamber, the one end that the cooling chamber was kept away from to the connecting pipe runs through fixed plate one and communicates with the hair-dryer, the one end that the hydrolysis furnace body was kept away from to the cooling chamber is provided with the air-cooler, the one end that the cooling chamber was kept away from to the air-cooler is connected with the air-cooler admission line, the one end that the air-cooler was close to the connecting pipe is.
Preferably, the surface of the feeding pipe is provided with a regulating valve.
Preferably, the cooling pipe is formed by communicating a plurality of bent pipes and straight pipes and is positioned on the same horizontal plane.
Preferably, the four fixing seats are all trapezoidal bodies with the same shape and size.
Preferably, the air inlet pipe and the air outlet pipe are both vertically connected with the hydrolysis furnace body.
Preferably, the circulating pipe is U-shaped and is vertically connected with the air outlet pipe.
Preferably, a filter screen is arranged inside one end of the circulating pipe, which is contacted with the air outlet pipe.
Preferably, the air cooler exhaust pipeline, the circulating pipe and the connecting pipe are communicated with the cooling chamber.
The invention provides a silicon dioxide hydrolysis furnace for producing rubber and plastic sealing elements. The method has the following beneficial effects:
(1) according to the invention, the air cooler is started, the air cooler conveys cold air into the cooling chamber through the air cooler exhaust pipeline, the blower is started, the blower absorbs the cold air and enters the hydrolysis furnace body from the air inlet pipe along the air outlet pipe to cool the silicon dioxide in the cooling chamber, then the air with heat is filtered by the filter screen and enters the cooling chamber along the circulating pipe to be cooled again, and then the blower conveys the air after being cooled again into the hydrolysis furnace body from the air inlet pipe along the air outlet pipe to be cooled to form circulation, so that the air with high heat can not be directly discharged into the air, thereby causing heat energy pollution to the environment, enabling the air to be recycled, and increasing the practicability of the device.
(2) According to the invention, the silicon dioxide is injected from the feeding pipe, so that the silicon dioxide is subjected to heat exchange through the cooling pipe and then discharged from the discharging pipe, the time for heat exchange between the silicon dioxide and the hydrolysis furnace body is prolonged, the heat exchange area is enlarged, the high-temperature silicon dioxide can be cooled to the required temperature, the influence on the next process due to incomplete heat exchange is avoided, and the heat exchange efficiency is improved.
(3) The invention achieves the purpose of filtering dust in air or in the hydrolysis furnace body through the filter screen arranged in the circulating pipe, and solves the problems that the gas cooling is not thorough possibly due to long dust accumulation time, and the device is broken down possibly due to the influence on the device.
Drawings
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a side view of the present invention;
FIG. 3 is an enlarged schematic view of the present invention A;
FIG. 4 is an enlarged view of the present invention B.
In the figure: 1 hydrolysis furnace body, 2 inlet pipes, 3 governing valves, 4 cooling tubes, 5 discharging pipes, 6 bottom plates, 7 supporting legs, 8 fixing bases, 9 backup pads, 10 fixed plate one, 11 hair-dryers, 12 play tuber pipe, 13 intake pipes, 14 outlet ducts, 15 circulating pipes, 16 filter screens, 17 fixed plate two, 18 cooling chambers, 19 connecting pipes, 20 air-coolers, 21 air-cooler admission line, 22 air-cooler exhaust duct.
Detailed Description
As shown in fig. 1 to 4, the present invention provides a technical solution: a silicon dioxide hydrolysis furnace for producing rubber and plastic sealing elements comprises a hydrolysis furnace body 1, wherein the left side and the right side of the bottom of the hydrolysis furnace body 1 are fixedly connected with supporting plates 9 which can support the hydrolysis furnace body 1, the bottoms of the two supporting plates 9 are respectively provided with a bottom plate 6, the two supporting plates 9 are respectively positioned on the two sides of the bottom plate 6 and are respectively fixedly connected with the bottom plate 6, four corners of the bottom plate 6 are respectively and fixedly connected with supporting legs 7, the bottoms of the four supporting legs 7 are respectively and fixedly connected with a fixed seat 8, the four fixed seats 8 are trapezoidal bodies with the same shape and size, the device is more fixed by the four fixed seats 8 and is not easy to shake, a feeding pipe 2 is arranged at the top of the hydrolysis furnace body 1, a regulating valve 3 is arranged on the surface of the feeding pipe 2, the hydrolysis furnace comprises a hydrolysis furnace body 1, a cooling pipe 4 is arranged in the hydrolysis furnace body 1, the cooling pipe 4 is formed by mutually communicating a plurality of bent pipes and straight pipes and is positioned on the same horizontal plane, the time for heat exchange between silicon dioxide and the hydrolysis furnace body 1 is prolonged, the heat exchange area is also increased, high-temperature silicon dioxide can be cooled to a required temperature, the next process cannot be affected due to incomplete heat exchange, the heat exchange efficiency is improved, one end of a feeding pipe 2 penetrating into the hydrolysis furnace body 1 is connected with the cooling pipe 4, a discharging pipe 5 is arranged at the lower right corner of the bottom of the hydrolysis furnace body 1, one end of the discharging pipe 5, which is close to the hydrolysis furnace body 1, penetrates through the hydrolysis furnace body 1 and extends into the hydrolysis furnace body 1, one end of the cooling pipe 4, which is far away from the feeding pipe 2, is connected with the discharging pipe 5, one end of the discharging pipe 5, which is far, the air inlet pipe 13 penetrates through the hydrolysis furnace body 1 and extends to the inside of the hydrolysis furnace body 1, cooling air enters the hydrolysis furnace body 1 from the air inlet pipe 13 to perform heat exchange treatment on high-temperature silicon dioxide, a first fixing plate 10 is arranged at one end, close to the air inlet pipe 13, of the hydrolysis furnace body 1, the first fixing plate 10 is fixedly connected with the hydrolysis furnace body 1, the top of the first fixing plate 10 is fixedly connected with a blower 11, the output end of the blower 11 is fixedly connected with an air outlet pipe 12, one end, away from the blower 11, of the air outlet pipe 12 is connected with the air inlet pipe 13, an air outlet pipe 14 is arranged at the left lower end of the hydrolysis furnace body 1, heat-carrying gas after heat exchange is discharged from the air outlet pipe 14, the air inlet pipe 13 and the air outlet pipe 14 are both vertically connected with the hydrolysis furnace body 1, the air outlet, the circulating pipe 15 is U-shaped and is vertically connected with the air outlet pipe 14, a filter screen 16 is arranged inside one end of the circulating pipe 15, which is contacted with the air outlet pipe 14, the filter screen 16 achieves the purpose of filtering dust in air or in the hydrolysis furnace body, the problem that the dust accumulation time is long, which may cause incomplete gas cooling and possibly affect the device to cause device failure is solved, the circulating pipe 15 respectively penetrates through two supporting plates 9, a fixing plate II 17 is arranged at the bottom of the fixing plate I10, the fixing plate II 17 is fixedly connected with the hydrolysis furnace body 1, a cooling chamber 18 is fixedly connected with the top of the fixing plate II 17, one end of the circulating pipe 15, which is far away from the air outlet pipe 14, penetrates through the fixing plate II 17 and is communicated with the cooling chamber 18, a connecting pipe 19 is arranged at the top of the cooling chamber 18, one end of the connecting pipe 19, which is close to the cooling chamber, make the air form the circulation, the air that contains the high heat can not directly discharge in the air, thereby can cause the heat energy pollution to the environment, the air that makes can carry out cyclic utilization, the practicality of device has been increased, the one end that hydrolysis furnace body 1 was kept away from to cooling chamber 18 is provided with air-cooler 20, the one end that cooling chamber 18 was kept away from to air-cooler 20 is connected with air-cooler admission line 21, the one end that air-cooler 20 is close to connecting pipe 19 is connected with air-cooler exhaust duct 22, circulating pipe 15 and connecting pipe 19 all communicate with cooling chamber 18, can send out from cooling chamber 18 after making air cooling, the one end that air-cooler 20 was kept away from to air-cooler exhaust duct 22 is connected with cooling chamber 18.
When the air cooling device is used, silicon dioxide is injected from the feeding pipe 2, the silicon dioxide is subjected to heat exchange through the cooling pipe 4, then the silicon dioxide is discharged from the discharging pipe 5, the air cooler 20 is started, the air cooler 20 conveys cold air into the cooling chamber 18 through the air cooler exhaust pipeline 22, the blower 11 is started, the blower 11 absorbs the cold air, the cold air enters the hydrolysis furnace body 1 from the air inlet pipe 13 along the air outlet pipe 12 to cool the silicon dioxide in the cooling pipe 4, then the air with heat is filtered through the filter screen 16 and then enters the cooling chamber 18 along the circulating pipe 15 to be cooled again, and then the air cooled again is sent into the hydrolysis furnace body 1 from the air inlet pipe 13 along the air outlet pipe 12 by the blower 11 to be cooled, so.
In conclusion, the invention starts the air cooler 20, so that the air cooler 20 conveys cold air into the cooling chamber 18 through the air cooler exhaust duct 22, starts the blower 11, so that the blower 11 absorbs the cold air and enters the hydrolysis furnace body 1 from the air inlet pipe 13 along the air outlet pipe 12 to cool the silica in the cooling pipe 4, then the air with heat is filtered by the filter screen 16 and enters the cooling chamber 18 along the circulating pipe 15 to be cooled again, then the blower 11 conveys the air after being cooled again into the hydrolysis furnace body 1 from the air inlet pipe 13 along the air outlet pipe 12 to be cooled, so as to form circulation, so that the air with high heat cannot be directly discharged into the air, thereby causing heat pollution to the environment, enabling the air to be recycled, increasing the practicability of the device, and injecting the silica from the feeding pipe 2 to exchange heat through the cooling pipe 4, then discharge from discharging pipe 5, silicon dioxide and the time of the heat transfer in the stove body 1 hydrolysising have been increaseed, the area of heat transfer has also been increaseed, make high temperature silicon dioxide can cool down to required temperature, can not exert an influence to next process because the heat transfer is incomplete, the efficiency of heat transfer has been improved, through the filter screen 16 that sets up in circulating pipe 15 inside, the mesh of perhaps hydrolysising the inside dust of stove body 1 in the filtered air has been reached, it is incomplete to have solved dust accumulation time and probably lead to gas cooling for a long time, still can produce the problem that the influence leads to the device trouble to the device.
Claims (8)
1. The utility model provides a silica hydrolysis furnace for rubber and plastic sealing member production, includes hydrolysis furnace body (1), its characterized in that: the hydrolysis furnace comprises a hydrolysis furnace body (1), wherein supporting plates (9) are fixedly connected to the left side and the right side of the bottom of the hydrolysis furnace body (1), a bottom plate (6) is arranged at the bottom of each of the two supporting plates (9), the two supporting plates (9) are positioned on the two sides of the bottom plate (6) and are fixedly connected with the bottom plate (6) respectively, supporting legs (7) are fixedly connected to the four corners of the bottom plate (6), fixing seats (8) are fixedly connected to the bottoms of the supporting legs (7), an inlet pipe (2) is arranged at the top of the hydrolysis furnace body (1), the inlet pipe (2) penetrates through the hydrolysis furnace body (1) and extends into the hydrolysis furnace body (1), a cooling pipe (4) is arranged inside the hydrolysis furnace body (1), one end of the inlet pipe (2) penetrating into the hydrolysis furnace body (1) is connected with the cooling pipe (4), and a, the one end that discharging pipe (5) are close to hydrolysis furnace body (1) runs through hydrolysis furnace body (1) and extends to hydrolysis furnace body (1) inside, the one end that inlet pipe (2) were kept away from in cooling tube (4) is connected with discharging pipe (5), the one end that hydrolysis furnace body (1) was kept away from in discharging pipe (5) runs through bottom plate (6) and extends to bottom plate (6) outside, hydrolysis furnace body (1) upper right corner is provided with intake pipe (13), intake pipe (13) run through hydrolysis furnace body (1) and extend to hydrolysis furnace body (1) inside, the one end that hydrolysis furnace body (1) is close to intake pipe (13) is provided with fixed plate (10), fixed plate (10) and hydrolysis furnace body (1) fixed connection, fixed plate (10) top fixedly connected with hair-dryer (11), hair-dryer (11) output end fixedly connected with goes out tuber pipe (12), the one end that air-out pipe (12) kept away from hair-dryer (11) is connected with intake pipe (13), the lower left end of stove body (1) of hydrolysising is provided with outlet duct (14), the outlet duct (14) of telling runs through stove body (1) of hydrolysising and extends to inside stove body (1) of hydrolysising, the one end that stove body (1) of hydrolysising was kept away from in outlet duct (14) is connected with circulating pipe (15), circulating pipe (15) run through two backup pads (9) respectively, the bottom of fixed plate one (10) is provided with fixed plate two (17), fixed plate two (17) and the stove body (1) of hydrolysising fixed plate two (17) fixed connection, fixed plate two (17) top fixed connection has cooling chamber (18), the one end that outlet duct (14) was kept away from in circulating pipe (15) runs through fixed plate two (17) and communicates with cooling chamber (18), cooling chamber (18, one end that connecting pipe (19) are close to cooling chamber (18) and cooling chamber (18) intercommunication, the one end that cooling chamber (18) were kept away from in connecting pipe (19) runs through fixed plate (10) and communicates with hair-dryer (11), the one end that hydrolysis furnace body (1) was kept away from in cooling chamber (18) is provided with air-cooler (20), the one end that cooling chamber (18) were kept away from in air-cooler (20) is connected with air-cooler admission line (21), the one end that air-cooler (20) are close to connecting pipe (19) is connected with air-cooler exhaust duct (22), the one end that air-cooler (20) were kept away from in air-cooler exhaust duct (22) is connected with cooling chamber (18).
2. The silica hydrolysis furnace for rubber and plastic seal production according to claim 1, wherein: the surface of the feeding pipe (2) is provided with a regulating valve (3).
3. The silica hydrolysis furnace for rubber and plastic seal production according to claim 1, wherein: the cooling pipe (4) is formed by mutually communicating a plurality of bent pipes and straight pipes and is positioned on the same horizontal plane.
4. The silica hydrolysis furnace for rubber and plastic seal production according to claim 1, wherein: the four fixing seats (8) are all trapezoidal bodies with the same shape and size.
5. The silica hydrolysis furnace for rubber and plastic seal production according to claim 1, wherein: the gas inlet pipe (13) and the gas outlet pipe (14) are both vertically connected with the hydrolysis furnace body (1).
6. The silica hydrolysis furnace for rubber and plastic seal production according to claim 1, wherein: the circulating pipe (15) is U-shaped and is vertically connected with the air outlet pipe (14).
7. The silica hydrolysis furnace for rubber and plastic seal production according to claim 6, wherein: a filter screen (16) is arranged in one end of the circulating pipe (15) which is contacted with the air outlet pipe (14).
8. The silica hydrolysis furnace for rubber and plastic seal production according to claim 1, wherein: and the air cooler exhaust pipeline (22), the circulating pipe (15) and the connecting pipe (19) are communicated with the cooling chamber (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911156308.4A CN110844909A (en) | 2019-11-22 | 2019-11-22 | Silicon dioxide hydrolysis furnace for producing rubber and plastic sealing elements |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911156308.4A CN110844909A (en) | 2019-11-22 | 2019-11-22 | Silicon dioxide hydrolysis furnace for producing rubber and plastic sealing elements |
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| Publication Number | Publication Date |
|---|---|
| CN110844909A true CN110844909A (en) | 2020-02-28 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201911156308.4A Pending CN110844909A (en) | 2019-11-22 | 2019-11-22 | Silicon dioxide hydrolysis furnace for producing rubber and plastic sealing elements |
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Citations (6)
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|---|---|---|---|---|
| CN201434600Y (en) * | 2009-06-01 | 2010-03-31 | 苏州中门子科技有限公司 | Strong cyclic rapid cooling chamber |
| US20150082818A1 (en) * | 2013-09-26 | 2015-03-26 | Carrier Corporation | System and method of freeze protection of a heat exchanger in an hvac system |
| CN205856011U (en) * | 2016-03-31 | 2017-01-04 | 久江控股集团有限公司 | It is provided with the silicon dioxide hydrolysis stove of spiral type heat exchange runner |
| CN206454450U (en) * | 2017-02-14 | 2017-09-01 | 河北洁净环保科技有限公司 | A kind of good condenser for fume treatment of condensation effect |
| CN207610553U (en) * | 2017-12-14 | 2018-07-13 | 西安奥邦科技有限责任公司 | A kind of water cooling plant of intermediate frequency furnace |
| CN108627024A (en) * | 2018-04-23 | 2018-10-09 | 成都立创创新科技有限公司 | A kind of steam exhaust condensate collection device that cooling water is recyclable |
-
2019
- 2019-11-22 CN CN201911156308.4A patent/CN110844909A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201434600Y (en) * | 2009-06-01 | 2010-03-31 | 苏州中门子科技有限公司 | Strong cyclic rapid cooling chamber |
| US20150082818A1 (en) * | 2013-09-26 | 2015-03-26 | Carrier Corporation | System and method of freeze protection of a heat exchanger in an hvac system |
| CN205856011U (en) * | 2016-03-31 | 2017-01-04 | 久江控股集团有限公司 | It is provided with the silicon dioxide hydrolysis stove of spiral type heat exchange runner |
| CN206454450U (en) * | 2017-02-14 | 2017-09-01 | 河北洁净环保科技有限公司 | A kind of good condenser for fume treatment of condensation effect |
| CN207610553U (en) * | 2017-12-14 | 2018-07-13 | 西安奥邦科技有限责任公司 | A kind of water cooling plant of intermediate frequency furnace |
| CN108627024A (en) * | 2018-04-23 | 2018-10-09 | 成都立创创新科技有限公司 | A kind of steam exhaust condensate collection device that cooling water is recyclable |
Non-Patent Citations (1)
| Title |
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| 兰永强等: "《分离生物乙醇用渗透汽化复合膜》", 31 July 2018 * |
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Application publication date: 20200228 |