CN111854470A - Chemical production reaction water heat recovery utilizes system - Google Patents
Chemical production reaction water heat recovery utilizes system Download PDFInfo
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- CN111854470A CN111854470A CN202010776019.0A CN202010776019A CN111854470A CN 111854470 A CN111854470 A CN 111854470A CN 202010776019 A CN202010776019 A CN 202010776019A CN 111854470 A CN111854470 A CN 111854470A
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- water
- box body
- spiral
- pipe
- chemical production
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/02—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
- F28D7/024—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
- F28F19/01—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using means for separating solid materials from heat-exchange fluids, e.g. filters
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/10—Energy recovery
Abstract
The invention provides a heat recycling system for chemical production reaction water. Chemical production reaction water heat recovery utilizes system includes: a base; the box body is fixedly connected with the upper surface of the base through the upright post; the reaction water inlet mechanism is connected with the upper surface of the box body; the heat exchange mechanism is connected with the box body and comprises a spiral water channel, a first spiral connector, a water outlet pipe, a water inlet pipe, a belt, a driving wheel, a driven wheel, a second rotary connector and a motor, wherein the spiral water channel is fixedly connected in the box body, one end of the spiral water channel is connected with the water outlet pipe, and the water outlet pipe penetrates through the box body and is in rotary sealing connection with the box body through the first spiral connector; the other end of the spiral water channel is connected with a water inlet pipe. The chemical production reaction water heat recycling system provided by the invention has the advantage of high heat exchange efficiency.
Description
Technical Field
The invention relates to the field of waste heat utilization, in particular to a chemical production reaction water heat recycling system.
Background
The chemical production process refers to a production process of chemically processing raw materials to finally obtain valuable products. Due to the diversity of raw materials and products and the complexity of the production process, tens of thousands of chemical production processes are formed. Throughout the various and complicated chemical production processes, the chemical reactions and a plurality of physical operations are organically combined. The chemical reaction and the reactor are the core of chemical production, and the physical process plays a role in preparing proper reaction conditions for the chemical reaction and separating and purifying reactants to obtain a final product.
In the chemical production process, the produced reaction water generally has heat, and when the heat of the chemical production reaction water is recycled at present, the heat exchange pipeline is fixedly arranged, and the water in the heat exchange pipeline can only exchange heat with the chemical production reaction water near the heat exchange pipeline, so that the heat exchange efficiency is influenced.
Therefore, there is a need to provide a new system for recycling the heat of the reaction water in chemical production to solve the above-mentioned technical problems.
Disclosure of Invention
In order to solve the technical problem, the invention provides a chemical production reaction water heat recycling system with high heat exchange efficiency.
The invention provides a chemical production reaction water heat recycling system, which comprises: a base; the box body is fixedly connected with the upper surface of the base through the upright post; the reaction water inlet mechanism is connected with the upper surface of the box body; the heat exchange mechanism is connected with the box body and comprises a spiral water channel, a first spiral connector, a water outlet pipe, a water inlet pipe, a belt, a driving wheel, a driven wheel, a second rotary connector and a motor, wherein the spiral water channel is fixedly connected in the box body, one end of the spiral water channel is connected with the water outlet pipe, and the water outlet pipe penetrates through the box body and is in rotary sealing connection with the box body through the first spiral connector; the other end of the spiral water channel is connected with a water inlet pipe, the water inlet pipe penetrates through the box body and is in rotary sealing connection with the box body through a second rotary connector, and the outer surface of the water inlet pipe is fixedly connected with a driven wheel; the upper surface of the base is fixedly connected with a motor, the output end of the motor is fixedly connected with a rotating center at one side of a driving wheel, and the driving wheel is in transmission connection with a driven wheel through a belt; a plurality of metal expansion wings are sleeved along the spiral water channel in a segmented manner, each expansion wing consists of a left buckling arc-shaped half pipe and a right buckling arc-shaped half pipe, the radian of the axis of each expansion wing is matched with the radian of the axis of the spiral water channel, the expansion wings can rotate around the axis of the spiral water channel, the wing length of each expansion wing is greater than one half of the pitch of the spiral water channel, and the radian corresponding to the axis of each expansion wing is greater than 40 degrees and less than 170 degrees; and the reaction water outlet mechanism is connected with the bottom of the box body.
Preferably, the reaction water inlet mechanism comprises a filter screen, a liquid inlet pipe, a filter box, a fixing plate, a bracket, a spring and a connecting pipe, wherein the upper surface of the box body is fixedly connected with the filter box through the bracket, the upper surface of the filter box is fixedly connected with the liquid inlet pipe communicated with the interior of the filter box, and the lower surface of the filter box is communicated with the box body through the connecting pipe; the filter box is internally provided with a filter screen which is matched with the filter box, a fixing plate is arranged below the filter screen, and the fixing plate is connected with the filter screen through a spring.
Preferably, reaction water inlet mechanism still includes first sealing door, the preceding terminal surface of rose box rotates and is connected with the first sealing door that matches the setting.
Preferably, the reaction water inlet mechanism further comprises a grid plate, the filter box is internally and fixedly connected with the grid plate, and the grid plate is positioned above the filter screen.
Preferably, the reaction water outlet mechanism comprises a liquid outlet pipe, a purified water tank, an activated carbon layer, a biofilm layer, a drain pipe, a flow guide pipe and a water pump, wherein the bottom of the tank body is fixedly connected with the drain pipe which is mutually communicated with the interior of the tank body; the water purification case and base fixed connection, and install the activated carbon layer and the biomembrane layer that are used for the water purification in the water purification case, the activated carbon layer is located biomembrane layer's top, and the bottom fixedly connected with of water purification case and the inside drain pipe that communicates each other of it.
Preferably, the reaction effluent mechanism further comprises an ultraviolet disinfection lamp, and a plurality of ultraviolet disinfection lamps are fixedly connected in the water purification tank.
Preferably, the reaction effluent mechanism further comprises a second sealing door, and the front end face of the purified water tank is rotatably connected with the second sealing door which is arranged in a matched mode.
Preferably, the front end face of the box body is rotatably connected with an access door which is arranged in a matched mode.
Compared with the related technology, the chemical production reaction water heat recycling system provided by the invention has the following beneficial effects:
1. the invention can recycle the waste heat in the reaction water of chemical production, thereby improving the resource utilization rate;
2. the spiral water channel can increase the travel of the normal-temperature water in the box body and increase the heat exchange time of the normal-temperature water and the chemical production reaction water, so that the heat exchange efficiency is improved;
3. according to the invention, the motor works, the driving wheel drives the driven wheel to rotate under the action of the belt, so that the water inlet pipe and the spiral water channel are driven to rotate, the chemical production reaction water in the box body can be disturbed through the rotation of the spiral water channel, and the normal-temperature water in the spiral water channel can exchange heat with the chemical production reaction water at different positions in the box body, so that the heat exchange between the normal-temperature water in the spiral water channel and the chemical production reaction water in the box body is facilitated, and the heat exchange efficiency is further improved; the rotatable extension wing that cup joints on the spiral water course can increase heat exchange and water to adjusting, and the extension wing of spiral water course different positions department is rotatory to different angles, can realize the regulation of the size and the angle in space between the spiral water course, also accessible rotatory extension wing closes the clearance between the spiral water course, has increased the regulation of the more directions of heat adjustable sensitivity and rivers.
4. According to the invention, after the water body is primarily purified by the activated carbon layer, secondary purification is carried out by the biological film layer, so that the difficulty of subsequent treatment of the water body is reduced, and even the water body can be directly discharged, thereby reducing the water body treatment cost of a user, avoiding the pollution to the environment and ensuring that the device is more environment-friendly.
Drawings
FIG. 1 is a schematic structural diagram of a preferred embodiment of a system for recycling heat of reaction water in chemical production according to the present invention;
FIG. 2 is a schematic view of a partial structure of the heat recycling system for chemical production reaction water shown in FIG. 1;
FIG. 3 is a schematic structural diagram of a reaction water inlet mechanism shown in FIG. 1;
FIG. 4 is a schematic diagram of an axial structure of the heat recovery system for chemical production reaction water shown in FIG. 1;
FIG. 5 is an enlarged view of a portion of FIG. 4 at A;
FIG. 6 is a schematic cross-sectional view of a spiral waterway with extended wings.
Reference numbers in the figures: 1. a reaction water inlet mechanism; 11. a filter screen; 12. a first sealing door; 13. a grid mesh panel; 14. a liquid inlet pipe; 15. a filter box; 16. a fixing plate; 17. a support; 18. a spring; 19. a connecting pipe; 2. a box body; 3. a base; 4. a reaction water outlet mechanism; 41. a liquid outlet pipe; 42. a water purifying tank; 43. an activated carbon layer; 44. a biofilm layer; 45. a drain pipe; 46. a second sealing door; 47. an ultraviolet disinfection lamp; 48. a flow guide pipe; 49. a water pump; 5. a heat exchange mechanism; 51. a spiral water channel; 52. a first screw connector; 53. a water outlet pipe; 54. a water inlet pipe; 55. a belt; 56. a driving wheel; 57. a driven wheel; 58. a second rotary connector; 59. an electric motor; 6. an access door; 7. and (4) a column.
Detailed Description
The invention is further described with reference to the following figures and embodiments.
Please refer to fig. 1, fig. 2, fig. 3, fig. 4, fig. 5 and fig. 6 in combination, in which fig. 1 is a schematic structural diagram of a heat recycling system for chemical production reaction water according to a preferred embodiment of the present invention; FIG. 2 is a schematic view of a partial structure of the heat recycling system for chemical production reaction water shown in FIG. 1; FIG. 3 is a schematic structural diagram of a reaction water inlet mechanism shown in FIG. 1; FIG. 4 is a schematic diagram of an axial structure of the heat recovery system for chemical production reaction water shown in FIG. 1; fig. 5 is a partial enlarged view of a portion a in fig. 4. Chemical production reaction water heat recovery utilizes system includes: a base 3; the box body 2 is fixedly connected with the upper surface of the base 3 through an upright post 7; the reaction water inlet mechanism 1 is connected with the upper surface of the box body 2; the heat exchange mechanism 5 is connected with the box body 2; and the reaction water outlet mechanism 4 is connected with the bottom of the box body 2.
In a specific implementation process, as shown in fig. 1, fig. 2, fig. 4 and fig. 5, the heat exchange mechanism 5 includes a spiral water channel 51, a first spiral connector 52, a water outlet pipe 53, a water inlet pipe 54, a belt 55, a driving wheel 56, a driven wheel 57, a second rotary connector 58 and a motor 59, the spiral water channel 51 is fixedly connected in the box body 2, one end of the spiral water channel 51 is connected with the water outlet pipe 53, and the water outlet pipe 53 penetrates through the box body 2 and is connected with the box body 2 in a rotary sealing manner through the first spiral connector 52; the other end of the spiral water channel 51 is connected with a water inlet pipe 54, the water inlet pipe 54 penetrates through the box body 2 and is connected with the box body 2 in a rotating and sealing mode through a second rotating connector 58, and a driven wheel 57 is fixedly connected to the outer surface of the water inlet pipe 54; the upper surface of the base 3 is fixedly connected with a motor 59, the output end of the motor 59 is fixedly connected with the rotating center of one side of the driving wheel 56, and the driving wheel 56 is in transmission connection with the driven wheel 57 through a belt 55.
Along the extension wing 21 of spiral water course 51 segmentation cup jointed a plurality of metal material, the extension wing 21 comprises the half pipe of buckle formula arc about by, the axis radian of every extension wing 21 and the axis radian phase-match of spiral water course 51, promptly, every extension wing 21 is also the spiral, the extension wing 21 can rotate around the axis of spiral water course 51, the wing length of extension wing 21 is greater than half of spiral water course 51 pitch, the radian that the axis of extension wing 21 corresponds is greater than 90 degrees and is less than 180 degrees. The wing 21 that expands has the arc half-pipe and welds the extension wing on the arc half-pipe, can increase the heat exchange of spiral water course 51 and reaction water, can adjust the angle of arc half-pipe on spiral water course 51 before the wing 21 is expanded in the installation, adjusts two expansion wings about fixed through the buckle after good. The rotatable extension wing that cup joints on the spiral water course can increase heat exchange and water to adjusting, and the extension wing of spiral water course different positions department is rotatory to different angles, can realize the regulation of the size and the angle in space between the spiral water course, also accessible rotatory extension wing closes the clearance between the spiral water course, has increased the regulation of the more directions of heat adjustable sensitivity and rivers.
When the device is used, reaction water with heat in chemical production enters the box body 2 through the reaction water inlet mechanism 1 and is finally discharged through the reaction water outlet mechanism 4; in normal temperature water enters into spiral water channel 51 through inlet tube 54, in box 2, the normal temperature water that has thermal chemical production reaction water and spiral water channel 51 carries out thermal exchange, and the normal temperature water in the heating spiral water channel 51 becomes hot water through the normal temperature water after the heat exchange, through outlet pipe 53 discharge hot water to can recycle the waste heat in the chemical production reaction water, improve resource utilization.
The spiral water channel 51 can increase the travel of the normal-temperature water in the box body 2 and increase the heat exchange time of the normal-temperature water and the chemical production reaction water, thereby improving the heat exchange efficiency; and work through motor 59, under the effect of belt 55, make action wheel 56 drive from driving wheel 54 rotation, thereby drive inlet tube 54 and spiral water course 51 and rotate, the chemical production reaction water in the box 2 can be disturbed in the rotation through spiral water course 51, normal atmospheric temperature water in the spiral water course 51 can carry out heat exchange with the chemical production reaction water of different positions in the box 2, be favorable to the heat exchange of normal atmospheric temperature water in the spiral water course 51 and the chemical production reaction water of internalizing in the box 2, further improve heat exchange's efficiency.
Referring to fig. 1 and 3, the reaction water inlet mechanism 1 includes a filter screen 11, a liquid inlet pipe 14, a filter tank 15, a fixing plate 16, a bracket 17, a spring 18 and a connecting pipe 19, the upper surface of the box body 2 is fixedly connected with the filter tank 15 through the bracket 17, the upper surface of the filter tank 15 is fixedly connected with the liquid inlet pipe 14 communicated with the inside of the filter tank 15, and the lower surface of the filter tank 15 is communicated with the box body 2 through the connecting pipe 19; the filter box 15 is internally provided with a filter screen 11 which is arranged in a matching way, a fixing plate 16 is arranged below the filter screen 11, and the fixing plate 16 is connected with the filter screen 11 through a spring 18.
Need to explain: chemical production reaction water enters into rose box 15 through feed liquor pipe 14 in, filters the back through filter screen 11, and rethread connecting pipe 19 enters into box 2, can avoid filter screen 11 chemical production reaction water in great impurity go into box 2 through filter screen 11 in, avoid great impurity to strike spiral water course 51 and cause the damage to spiral water course 51, improve the reliability that the device used.
The spring 18 can buffer the impact force of the water flow and the filter screen 11, and reduce the damage probability of the filter screen 11.
Referring to fig. 3, the reaction water inlet mechanism 1 further includes a first sealing door 12, and the front end surface of the filter box 15 is rotatably connected with the first sealing door 12 which is arranged in a matching manner. The filter box 15 is cleaned by opening the first sealing door 12, and the working difficulty of operators is reduced.
Referring to fig. 3, the reaction water inlet mechanism 1 further includes a grid plate 13, the grid plate 13 is fixedly connected in the filter box 15, and the grid plate 13 is located above the filter screen 11. Can block rivers through grid plate 13, avoid rivers direct impact filter screen 11, further reduce the probability that filter screen 11 damaged, can reduce the velocity of flow when rivers pass through filter screen 11 simultaneously through grid plate 13, improve the filter effect of filter screen 11 to rivers.
Referring to fig. 1 and 4, the reaction effluent mechanism 4 comprises an effluent pipe 41, a purified water tank 42, an activated carbon layer 43, a biofilm layer 44, a drain pipe 45, a draft tube 48 and a water pump 49, wherein the bottom of the tank 2 is fixedly connected with the drain pipe 45 communicated with the interior of the tank, one end of the drain pipe 45 far away from the tank 2 is connected with a water inlet of the water pump 49, a water outlet of the water pump 49 is connected with one end of the draft tube 48, and the other end of the draft tube 48 is connected with a water inlet close to the top of the purified water tank 42; the water purification tank 42 is fixedly connected with the base 3, an activated carbon layer 43 and a biological membrane layer 44 for purifying water are installed in the water purification tank 42, the activated carbon layer 43 is located above the biological membrane layer 44, and the bottom of the water purification tank 42 is fixedly connected with a drain pipe 45 communicated with the interior of the water purification tank. The biofilm layer 44 is a ceramic filler with honeycomb holes, and the surface of the ceramic filler is loaded with a biofilm consisting of microorganisms, so that the water body is purified through the biofilm.
Through the work of water pump 49, can send into the purifying box 42 through honeycomb duct 48 with the chemical production reaction water after carrying out the heat exchange in the box 2 in, carry out preliminary purification back to the water through activated carbon layer 43, rethread biofilm layer 44 carries out the secondary and purifies, and the degree of difficulty that reduces water follow-up treatment can directly discharge even to reduce user's water treatment cost, avoid the pollution to the environment simultaneously, make the device environmental protection more.
Referring to fig. 1, the reaction effluent mechanism 4 further includes an ultraviolet disinfection lamp 47, and a plurality of ultraviolet disinfection lamps 47 are fixedly connected in the purified water tank 42. The water body can be sterilized by ultraviolet rays through the ultraviolet disinfection lamps 47, and the water body purification effect is improved.
Referring to fig. 1, the reaction effluent outlet mechanism 4 further comprises a second sealing door 46, and the front end surface of the purified water tank 42 is rotatably connected with the second sealing door 46 which is arranged in a matching manner. The second sealing door 46 is opened to facilitate cleaning of the fresh water tank 42, thereby reducing the burden on the user.
Referring to fig. 1, an access door 6 is rotatably connected to the front end surface of the box body 2. Cleaning of the interior of the cabinet 2 is facilitated by opening the access door 6.
The above description is only an embodiment of the present invention, and not intended to limit the scope of the present invention, and all modifications of equivalent structures and equivalent processes, which are made by using the contents of the present specification and the accompanying drawings, or directly or indirectly applied to other related technical fields, are included in the scope of the present invention.
Claims (8)
1. A chemical production reaction water heat recycling system is characterized by comprising:
a base (3);
the box body (2) is fixedly connected with the upper surface of the base (3) through an upright post (7);
the reaction water inlet mechanism (1), the reaction water inlet mechanism (1) is connected with the upper surface of the box body (2);
the heat exchange device comprises a heat exchange mechanism (5), wherein the heat exchange mechanism (5) is connected with the box body (2), the heat exchange mechanism (5) comprises a spiral water channel (51), a first spiral connector (52), a water outlet pipe (53), a water inlet pipe (54), a belt (55), a driving wheel (56), a driven wheel (57), a second rotary connector (58) and a motor (59), the spiral water channel (51) is fixedly connected in the box body (2), one end of the spiral water channel (51) is connected with the water outlet pipe (53), and the water outlet pipe (53) penetrates through the box body (2) and is connected with the box body (2) in a rotating and sealing mode through the first spiral connector (52); the other end of the spiral water channel (51) is connected with a water inlet pipe (54), the water inlet pipe (54) penetrates through the box body (2) and is connected with the box body (2) in a rotating and sealing mode through a second rotating connector (58), and a driven wheel (57) is fixedly connected to the outer surface of the water inlet pipe (54); the upper surface of the base (3) is fixedly connected with a motor (59), the output end of the motor (59) is fixedly connected with the rotating center of one side of a driving wheel (56), the driving wheel (56) is in transmission connection with a driven wheel (57) through a belt (55), a plurality of metal expansion wings (21) are sleeved along the spiral water channel (51) in a segmented mode, each expansion wing (21) consists of a left buckling type arc half pipe and a right buckling type arc half pipe, the radian of the axis of each expansion wing (21) is matched with the radian of the axis of the spiral water channel (51), the expansion wings (21) can rotate around the axis of the spiral water channel (51), the wing length of each expansion wing (21) is larger than a half of the pitch of the spiral water channel (51), and the radian corresponding to the axis of each expansion wing (21) is larger than 40 degrees and smaller than 170 degrees;
and the reaction water outlet mechanism (4) is connected with the bottom of the box body (2).
2. The heat recycling system for the reaction water in the chemical production according to claim 1, wherein the reaction water inlet mechanism (1) comprises a filter screen (11), a liquid inlet pipe (14), a filter box (15), a fixing plate (16), a support (17), a spring (18) and a connecting pipe (19), the upper surface of the box body (2) is fixedly connected with the filter box (15) through the support (17), the upper surface of the filter box (15) is fixedly connected with the liquid inlet pipe (14) communicated with the interior of the filter box, and the lower surface of the filter box (15) is communicated with the box body (2) through the connecting pipe (19); the filter box (15) is internally provided with a filter screen (11) which is arranged in a matching way, a fixing plate (16) is arranged below the filter screen (11), and the fixing plate (16) is connected with the filter screen (11) through a spring (18).
3. The chemical production reaction water heat recycling system according to claim 2, wherein the reaction water inlet mechanism (1) further comprises a first sealing door (12), and the front end surface of the filter box (15) is rotatably connected with the first sealing door (12) which is arranged in a matching manner.
4. The chemical production reaction water heat recycling system according to claim 2, wherein the reaction water inlet mechanism (1) further comprises a grid plate (13), the filter box (15) is internally and fixedly connected with the grid plate (13), and the grid plate (13) is positioned above the filter screen (11).
5. The system for recycling the heat of the reaction water in the chemical production according to claim 1, wherein the reaction water outlet mechanism (4) comprises a liquid outlet pipe (41), a water purification tank (42), an activated carbon layer (43), a biofilm layer (44), a water outlet pipe (45), a flow guide pipe (48) and a water pump (49), the bottom of the tank body (2) is fixedly connected with the water outlet pipe (45) which is communicated with the interior of the tank body, one end of the water outlet pipe (45) far away from the tank body (2) is connected with a water inlet of the water pump (49), a water outlet of the water pump (49) is connected with one end of the flow guide pipe (48), and the other end of the flow guide pipe (48) is connected with a water inlet close to; water purification case (42) and base (3) fixed connection, and install activated carbon layer (43) and biofilm layer (44) that are used for the water purification in water purification case (42), activated carbon layer (43) are located the top of biofilm layer (44), and the bottom fixedly connected with of water purification case (42) and inside drain pipe (45) of intercommunication each other.
6. The chemical production reaction water heat recycling system according to claim 5, wherein the reaction water outlet mechanism (4) further comprises a plurality of ultraviolet disinfection lamps (47), and a plurality of ultraviolet disinfection lamps (47) are fixedly connected in the purified water tank (42).
7. The chemical production reaction water heat recycling system according to claim 5, wherein the reaction water outlet mechanism (4) further comprises a second sealing door (46), and the front end surface of the purified water tank (42) is rotatably connected with the second sealing door (46) which is arranged in a matching manner.
8. The chemical production reaction water heat recycling system according to claim 1, wherein the front end face of the box body (2) is rotatably connected with an access door (6) which is arranged in a matching manner.
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| CN202010776019.0A CN111854470A (en) | 2020-08-05 | 2020-08-05 | Chemical production reaction water heat recovery utilizes system |
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| CN202010776019.0A CN111854470A (en) | 2020-08-05 | 2020-08-05 | Chemical production reaction water heat recovery utilizes system |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20030212150A1 (en) * | 1999-11-26 | 2003-11-13 | Bp Exploration Operating Company Limited | Process for converting synthesis gas into higher hydrocarbons |
| CN101876514A (en) * | 2009-10-30 | 2010-11-03 | 绍兴永利环保科技有限公司 | Energy-saving waste liquid heat exchange treatment device |
| CN206523076U (en) * | 2016-05-12 | 2017-09-26 | 北京住总商品混凝土中心 | A kind of waste water heat recovering equipment |
| CN209069052U (en) * | 2018-11-22 | 2019-07-05 | 于慧佳 | A kind of environment-friendly type waste water thermal energy converter |
| CN209302469U (en) * | 2018-12-19 | 2019-08-27 | 高密浩翰木塑材料科技有限公司 | A kind of reaction kettle waste gas continuous purification processing unit |
| CN209569740U (en) * | 2018-12-29 | 2019-11-01 | 江苏天祺环保科技有限公司 | A kind of rto waste heat recycling storage equipment |
| CN210512744U (en) * | 2019-07-08 | 2020-05-12 | 安徽中能特种设备有限公司 | High-efficient spiral tube heat exchanger |
-
2020
- 2020-08-05 CN CN202010776019.0A patent/CN111854470A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20030212150A1 (en) * | 1999-11-26 | 2003-11-13 | Bp Exploration Operating Company Limited | Process for converting synthesis gas into higher hydrocarbons |
| CN101876514A (en) * | 2009-10-30 | 2010-11-03 | 绍兴永利环保科技有限公司 | Energy-saving waste liquid heat exchange treatment device |
| CN206523076U (en) * | 2016-05-12 | 2017-09-26 | 北京住总商品混凝土中心 | A kind of waste water heat recovering equipment |
| CN209069052U (en) * | 2018-11-22 | 2019-07-05 | 于慧佳 | A kind of environment-friendly type waste water thermal energy converter |
| CN209302469U (en) * | 2018-12-19 | 2019-08-27 | 高密浩翰木塑材料科技有限公司 | A kind of reaction kettle waste gas continuous purification processing unit |
| CN209569740U (en) * | 2018-12-29 | 2019-11-01 | 江苏天祺环保科技有限公司 | A kind of rto waste heat recycling storage equipment |
| CN210512744U (en) * | 2019-07-08 | 2020-05-12 | 安徽中能特种设备有限公司 | High-efficient spiral tube heat exchanger |
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Application publication date: 20201030 |