CN208349557U - A kind of multilayer hot water storage tank, thermal energy recycling and reusing system - Google Patents
A kind of multilayer hot water storage tank, thermal energy recycling and reusing system Download PDFInfo
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- CN208349557U CN208349557U CN201820685158.0U CN201820685158U CN208349557U CN 208349557 U CN208349557 U CN 208349557U CN 201820685158 U CN201820685158 U CN 201820685158U CN 208349557 U CN208349557 U CN 208349557U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 529
- 238000003860 storage Methods 0.000 title claims abstract description 117
- 238000004064 recycling Methods 0.000 title abstract description 31
- 238000000034 method Methods 0.000 claims abstract description 110
- 238000010438 heat treatment Methods 0.000 claims abstract description 39
- 238000004519 manufacturing process Methods 0.000 claims abstract description 27
- 238000009413 insulation Methods 0.000 claims abstract description 18
- 238000011084 recovery Methods 0.000 claims description 31
- 238000010521 absorption reaction Methods 0.000 claims description 28
- 239000008213 purified water Substances 0.000 claims description 24
- 238000005265 energy consumption Methods 0.000 abstract description 14
- 238000000746 purification Methods 0.000 abstract description 6
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- 238000002347 injection Methods 0.000 abstract 1
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- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 12
- 239000000126 substance Substances 0.000 description 11
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- 238000004821 distillation Methods 0.000 description 9
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- 238000000605 extraction Methods 0.000 description 8
- 230000001105 regulatory effect Effects 0.000 description 8
- 238000001816 cooling Methods 0.000 description 7
- 230000017525 heat dissipation Effects 0.000 description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 6
- 239000002585 base Substances 0.000 description 6
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- 238000006386 neutralization reaction Methods 0.000 description 6
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Classifications
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
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- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
The utility model discloses a kind of multilayer hot water storage tanks comprising: successively nested inner canister, at least one pans and outer tank from inside to outside；Inner canister, pans and outer pot bottom are provided with water outlet；Inner canister, pans and outer tank are separated by thermal insulation layer；Inner canister, pans and outer tank are provided with temperature sensor；Inner canister, the through-hole that the tank skin of pans is equipped with are connected to the water in tank；Inner canister is equipped with heating tube；Outer tank is equipped with water inlet.The invention also discloses thermal energy recycling and reusing system and its reuse methods, and for recycling and reusing endothermic process and/or the thermal energy of exothermic process, using the multilayer hot water storage tank as heat source, the waste heat after heating returns to collection water pot；Multilayer hot water storage tank is then from collection water pot supplement water inlet；The water purification of the heat production caused by exothermic process, collecting injection preheating water purification storage tank for producing and using reduces energy consumption；Energy pipe is got up by these approach, is comprehensively utilized, total energy consumption can substantially reduce, and be suitable for being widely applied.
Description
Technical Field
The utility model belongs to the technical field of energy recovery recycles, concretely relates to multilayer hot water storage tank, heat recovery system of recycling.
Background
A chemical or chinese drug factory with multiple products consumes a large amount of energy in production, a large amount of which is heat energy. Heating is needed for chemical reaction, distillation of liquid, extraction of traditional Chinese medicine components, concentration of aqueous solution, evaporation of solvent and the like; meanwhile, some exothermic reactions require cooling to control the temperature, and processes such as fraction recovery, spray recovery of some volatile chemicals, and the like also require cooling. Also, for example, some product drying processes (e.g., ebullated bed dryers, spray dryers, etc.) generate large amounts of high temperature waste gases, and some process generate large amounts of high temperature waste water (e.g., distillation tower bath) with significant amounts of heat.
In general, each reaction or process is treated separately, for example, a reaction at 120 ℃, heated by steam, and the hot water condensed from the steam is generally put into a sewer, and the heat carried by the hot water is released into the environment. And cooling with water in an acid-base neutralization process, and discharging the cooled hot water into a sewer, wherein the discharged heat is not utilized, and the same amount of cold energy is used. High-temperature waste gas and waste water are also discharged at will. And so on, the energy loss due to the individual treatment of each reaction is considerable. Furthermore, what is more important is that sometimes the temperature is not controlled to the temperature required by the process, which affects the quality of the product or causes environmental pollution (for example, ammonia recovery is not low enough, ammonia recovery efficiency is affected, and ammonia is discharged to the polluted environment). In fact, the control temperature of different processes is different, the waste water of the high-temperature process can be completely used for heating at a lower temperature, and the heat released by exothermic chemical reaction is quite large and can be completely utilized. In a word, the energy is measured and comprehensively utilized, and the total energy consumption and the unit energy consumption of a factory can be greatly reduced.
SUMMERY OF THE UTILITY MODEL
In order to overcome the problems existing in the prior art, the utility model provides a multilayer hot water storage tank of innovative design, i.e. a korstech (TRUSTECH) multilayer hot water storage tank. The utility model also provides a heat recovery system of recycling and heat recovery method of recycling for the heat energy of heat absorption process and/or exothermal process is recycled.
The utility model provides a moral multilayer hot water storage tank, it includes: the inner tank, the at least one intermediate tank and the outer tank are sequentially nested from inside to outside; wherein, the center of the inner tank is provided with a heating pipe; the bottoms of the inner tank, the intermediate tank and the outer tank are respectively provided with a water outlet; a water inlet is formed in the outer wall of the outer tank; the tank walls of the inner tank and the intermediate tank are respectively provided with at least one through hole; the inner tank, the intermediate tank and the outer tank are respectively provided with a temperature sensor; the tank walls of the inner tank, the intermediate tank and the outer tank are heat insulation layers.
Wherein, the outer wall of the outer tank is provided with a heat-insulating layer. The outer tank is provided with a first liquid level sensor. And an emptying pipe is arranged at the top of the outer tank.
The inner tank, the intermediate tank and the outer tank are in the shapes of cylinders, cubes, spheres and the like, and can be in any other suitable shapes.
The inner tank and the intermediate tank are provided with holes on the tank walls for air to circulate between the adjacent tanks, so that the air in the multi-layer hot water storage tank is communicated.
Wherein, adjacent the water temperature difference between interior jar and the pans is 15 ~ 20 ℃, and the water temperature difference between adjacent pans and the outer jar is 15 ~ 20 ℃.
Preferably, in a specific embodiment, the water temperature of the inner tank is 95 ℃, the water temperature of the intermediate tank is 75-80 ℃, and the water temperature of the outer tank is 55-65 ℃.
The utility model also provides a heat recovery system of recycling for the heat energy that produces among the recovery heat absorption process of recycling, one kind is recycled the heat energy that the heat absorption process took place promptly, and it includes: the multi-layer hot water storage tank, the heat absorption process equipment with the jacket and the collection water tank; the water outlet of the multilayer hot water storage tank is communicated with the water inlet of the jacket through a pipeline; the water outlet of the jacket is communicated with the water inlet of the solar water heater through a pipeline, and the water inlet of the solar water heater is externally connected with softened pipeline water; the water outlet of the solar water heater is communicated with the water inlet of the water collecting tank through a pipeline; the water outlet of the collecting water tank is communicated with the water inlet of the multilayer hot water storage tank through a pipeline.
The utility model discloses in, endothermic process equipment is the equipment that has the heat absorption process to go on wherein, include: a reaction kettle for endothermic reaction, a traditional Chinese medicine extraction pot, a distillation tower heated by a jacket, a liquid concentration device, a solvent evaporator and other various devices.
The water collecting tank is provided with at least one water outlet. One water outlet of the collecting water tank is communicated with the water inlet of the multilayer hot water storage tank, and a pump is arranged between the water outlet and the water inlet.
Wherein the water collecting tank is provided with a vent/overflow. The collection water tank is provided with a second liquid level sensor. The outer wall of the water collecting tank is provided with a heat insulation layer, so that the loss of heat energy is avoided.
Further, the utility model discloses still provide another kind of heat recovery system of recycling, on the basis of the heat energy that the endothermic in-process of aforesaid recovery produced, further including the recovery of the heat energy that produces to exothermic in-process and recycle. The utility model provides a can retrieve and recycle the heat energy that the endothermic process takes place, can retrieve the heat energy that the exothermic process takes place again. The system further comprises, in addition to the heat energy recovery and reuse system of the endothermic process described above: a jacketed exothermic process unit, a heat exchanger, and a preheated clean water storage tank. Wherein, the heat exchanger is used for recovering the heat energy of the high-temperature waste gas and water.
Wherein, the water inlet of the jacket is externally connected with a water source such as purified water for production. And the water outlet of the jacket is communicated with the water inlet of the preheating purified water storage tank through a pipeline.
Wherein, the water inlet of the heat exchanger is externally connected with a water source such as purified water for production. And the water outlet of the heat exchanger is communicated with the water inlet of the preheating purified water storage tank through a pipeline.
Wherein, preheat the water purification storage tank and be equipped with at least one water inlet. The water inlet can be externally connected with a water source such as purified water for production. The water inlet can be communicated with the water outlet of the jacket. The water inlet can also be communicated with a water outlet of the heat exchanger.
Wherein, the preheating purified water storage tank is provided with at least one water outlet. The water outlet is communicated with the water inlet of the solar water heater through a pipeline.
The preheated water stored in the preheated purified water storage tank can flow out through the water outlet and is conveyed to the water inlet of the solar water heater through the pipeline to be provided as a water source, such as softened pipeline water. The waste water can also flow out through the water outlet and is used as production water, preferably production pure water, and the waste water is conveyed to endothermic process equipment to participate in reaction, so that the heat energy consumption in the endothermic process is further reduced. The water can also flow out through the water outlet to be used as the production water needed in other production links. Can also flow out through the water outlet and be used as domestic water.
Wherein, preheat the water purification storage tank and be equipped with drain/overflow mouth. The preheating purified water storage tank is provided with a third liquid level sensor. And the outer wall of the preheating purified water storage tank is provided with a heat insulation layer.
The utility model discloses in, exothermic process equipment is the equipment that carries out exothermic process, including carrying out various exothermic chemical reaction's various equipment such as the condenser of fraction in reation kettle, the distillation column.
The utility model discloses still provide a heat recovery method of recycling, utilize heat recovery system of recycling for the heat that produces in the heat absorption process is recycled, and it includes following step:
the water flowing through the jacket of the heat absorption process equipment has the temperature reduced, then flows through the solar water heater, has the temperature increased, and flows into the water collection tank. Or the softened water in the pipeline flows through the solar water heater, the temperature of the softened water rises and the softened water flows into the water collecting tank.
When the liquid level in the multilayer hot water storage tank descends to a certain degree, the pump controlled by the first liquid level sensor starts to work, the water in the collecting water tank is pumped into the water inlet of the multilayer hot water storage tank, the water enters the outer tank and flows into other tanks through the through holes in the tank wall, and the water circulates between the adjacent tanks.
The temperature of the water in the inner tank is regulated and controlled by heating the heating pipe.
According to the different temperatures required by the heat absorption process equipment, different regulating valves are selected, so that the water in the inner tank, the middle tank and/or the outer tank, namely the water with different temperatures, can flow out from the water outlet. Hot water of different temperatures selected as required flows into the jacket of the heat-absorbing process device, continuously providing heat to the heat-absorbing process device. After heat exchange, the water with reduced temperature in the jacket flows out through the jacket water outlet. The water flowing out is heated by flowing into a solar heater, the temperature is increased, and the water flows into a water collecting tank.
The whole system forms circulation, and heat energy can be recycled repeatedly and circularly, so that the production energy consumption is reduced to minimum.
Further, the utility model discloses heat recovery recycles method can also include the step of the produced heat of recovery recycle heat release process, still includes following step promptly:
water, preferably process clean water, flows into the jacket of the exothermic process equipment, exchanges heat, flows out of the jacket, and flows into the preheated clean water storage tank.
Alternatively, water, preferably clean process water, flows into the preheated clean water tank.
Or, water, preferably clean water for production, flows into a heat exchanger for recovering heat energy of high-temperature waste gas and waste water, and after heat exchange, the water with the increased temperature flows out of a water outlet of the heat exchanger and flows into a preheating clean water storage tank.
The water flows out from the preheating purified water storage tank, is communicated through a pipeline and flows into the solar heater. After flowing out from the solar heater, water enters the heat energy recycling process, and is recycled, so that the heat energy can be recycled, and the energy consumption is extremely low.
The water flows out from the preheating pure water storage tank, can be communicated through a pipeline and flows into the heat absorption process equipment to be used as production water or heat absorption reaction water. The production clean water to be heated in the heat absorption process equipment is taken from the preheating clean water storage tank, so that the heating energy consumption is further reduced.
The utility model provides a multilayer hot water storage tank, heat recovery system of recycling and heat recovery method of recycling, its beneficial effect includes: the energy is recovered and saved, and the unit energy consumption of the product is reduced. The temperature can be accurately controlled, the local temperature is prevented from being too high, the process requirement is favorably met, and the product quality is ensured. Because the size of the heat dissipation and the heat dissipation area is related to the temperature difference between the heat dissipation surface and the outside, the design of the multilayer hot water storage tank reduces the heat dissipation area, reduces the temperature of the heat dissipation surface and minimizes the heat loss. The design of the multilayer hot water storage tank only needs one heating pipe, and heating equipment is reduced. The design of the multilayer hot water storage tank only controls the water temperature of the heating inner storage tank, and temperature control equipment is reduced. The design of the multilayer hot water storage tank only needs one liquid level control system, and liquid level control equipment is reduced. The multilayer hot water storage tank is designed to have consistent hot water liquid level height of each tank, the space reserved above the multilayer hot water storage tank is small, and the nearly optimal volume utilization rate can be achieved.
The utility model discloses in, to every equipment, often require to reach the temperature of settlement in the short time, if with electric heating the electric power ratio great with regard to requiring equipment. The hot water storage tank can be used for heating the water storage tank for a long time in advance, and then the hot water is transmitted to the heat utilization equipment, so that the electric heating power can be reduced. Meanwhile, equipment cost can be saved because each piece of equipment does not need to be heated. And the system can utilize the valley to heat at night, thereby saving the expenditure and being beneficial to the balanced power generation of the whole power grid. The utility model discloses an aforementioned a plurality of ways get up the energy pipe, comprehensive utilization, and total energy consumption just can greatly reduced, is suitable for wide application.
The utility model adopts the multilayer hot water storage tank as a heat source to replace that only one energy source of steam (or electricity) is used for heating each heat absorption process, and the heated waste heat is returned to the water collection tank; the multilayer hot water storage tank is replenished with water from the water collecting tank; the heat generated in the heat release process can be used for heating the purified water for production, and the purified water is collected and injected into the preheated purified water storage tank for production use, so that the energy consumption is reduced; the energy is managed through the ways, the energy is comprehensively utilized, the total energy consumption can be greatly reduced, the method is suitable for wide application, the heat energy generated in the production and manufacturing process of the chemical and pharmaceutical industry is effectively recycled, the production energy consumption is greatly reduced, and a solution is provided for realizing environmental protection, greenness and energy consumption reduction in the large-scale chemical and pharmaceutical industry.
Drawings
Fig. 1 is a schematic structural view of the multi-layer hot water storage tank of the present invention.
Fig. 2a is a schematic cross-sectional view of the multi-layered hot water storage tank of the present invention.
Fig. 2b is a schematic cross-sectional view of another structure of the kder multilayer hot water storage tank of the present invention.
Fig. 3a is a schematic diagram of the heat energy recycling system of the present invention applied to heat energy recycling in the heat absorption process.
Fig. 3b is a schematic diagram of the heat energy recycling system of the present invention applied to heat energy recycling in the heat releasing process.
Detailed Description
The present invention will be described in further detail with reference to the following specific examples and the accompanying drawings. The procedures, conditions, experimental methods and the like for carrying out the present invention are general knowledge and common general knowledge in the art except for the contents specifically mentioned below, and the present invention is not particularly limited.
As shown in fig. 1-3, 1-inner vessel; 2-a tundish; 3-outer pot; 4-heating a tube; 5-water outlet; 6-a heat insulation layer; 7-a through hole; 8-a first level sensor; 9-a water inlet; 10-a blow-down pipe; 11-collecting a water tank; 111-emptying/overflow of the collecting tank; 112-a pump; 113-a second liquid level sensor; 12-a heat-absorbing process device; 13-exothermic process equipment; 14-a heat exchanger; 15-solar water heater; a-a jacket; b-a heat insulation layer; 16-preheating a purified water storage tank; 161-a third level sensor; 162-preheating the emptying/overflow of the clean water storage tank.
The utility model provides a multilayer hot water storage tank A, include: an inner tank 1, at least one intermediate tank 2 and an outer tank 3 are nested in sequence from inside to outside. As shown in fig. 1, fig. 2a and fig. 2b, the multi-layered hot water storage tank of the present invention includes an inner tank 1, an intermediate tank 2 and an outer tank 3.
The utility model discloses in the moral multilayer hot water storage tank, can store water in each jar. The shapes of the inner tank 1, the intermediate tank 2 and the outer tank 3 are not limited, and may be cylinders, cubes or any other suitable shapes. In a specific embodiment, the present invention may be a multilayer structure, as shown in fig. 2 a; it may also be a multi-layered jacketed structure, as shown in fig. 2 b.
The outer wall of the outer tank 3 is provided with a water inlet 9. Inner tank 1, pans 2, outer jar 3, the bottom of each jar respectively is equipped with delivery port 5, and through regulation and control valve switch, the water in each jar can flow out from the delivery port 5 that corresponds respectively, also can be the water in two or more jars flows out simultaneously.
The tank wall of the inner tank 1 and the tank wall of the intermediate tank 2 are respectively provided with a through hole 7, and a plurality of through holes 7 can be arranged. The through holes 7 communicate between two adjacent tanks, and allow water of different temperatures to flow between the inner tank 1 and the intermediate tank 2 adjacent thereto, between two adjacent intermediate tanks 2, and between the outer tank 3 and the intermediate tank 2 adjacent thereto.
The water level of a plurality of tanks in the multi-layer hot water storage tank is approximately equal through the through holes 7, and when any one tank outputs water outwards, the water of other tanks is supplemented through the through holes 7 until the water level of each tank is equal.
The tank walls of the inner tank 1, the intermediate tank 2 and the outer tank 3 are heat insulation layers 6, the heat insulation layers separate the inner tank 1 from the intermediate tank 2, the intermediate tank 2 from the outer tank 3 and the intermediate tank, and the heat insulation effect of the heat insulation layers 6 is that heat conduction between adjacent tanks is blocked to a certain extent, so that temperature difference is formed between the adjacent tanks, and stepped temperature difference is formed between the tanks. The through holes 7 allow water to flow between adjacent tanks, and the inner tank is replenished with water from the middle tank and heated to a set temperature by the heating pipe 4. The middle tank is supplemented with water from the inner tank and the outer tank at the same time, the water temperature of the inner tank is higher than that of the middle tank, the water temperature of the outer tank is lower than that of the middle tank, and the difference between the water temperature of the inner tank and that of the outer tank after mixing is little. The outer tank replenishes water from the middle tank and the water collecting tank, and the temperatures of the two types of water are balanced. Generally, since the amount of water in each hot water storage tank is large, the amount of water entering through the through holes 7 is relatively small, and the influence on the change of the water temperature in each tank is small.
The center of the inner tank 1 is provided with a heating pipe 4, and the water in the inner tank moves in an up-down convection circulation mode to transfer heat. The temperature of the water in the inner vessel 1 can be regulated by controlling the heating pipe 4 by means of the temperature sensor T1. The heating pipe 4 can be a steam-supplying pipe, an electric heating pipe or other suitable heating devices which can provide heat sources.
The inner tank 1 is a heating tank, and the temperature in the tank is highest. The wall of the inner tank 1 transfers part of the heat to the inner wall of the intermediate tank, which is the heat source of the intermediate tank water, and similarly, the wall between the intermediate tank and the outer tank is the heat source of the outer tank water. The water in the middle tank and the outer tank also transfers heat in a mode of up-down convection circulation. Water in each adjacent tank can flow through the through holes 7, and water does not flow much when water is not used, so that heat is less influenced by the heat transfer between the tanks. Preferably, the temperature of the intermediate tank 2 is lower than that of the inner tank 1, and the temperature of the outer tank 3 is lower than that of the intermediate tank 2, which configuration is most energy-saving. Preferably, the water temperature of the inner tank 1 can be set to 95 ℃, the temperature is gradually reduced through the heat insulation layer 6, the water temperature of the intermediate tank 2 is 75-80 ℃, and the water temperature of the outer tank 3 is 55-65 ℃.
The inner tank 1, the intermediate tank 2 and the outer tank 3 are respectively provided with a temperature sensor T, and the temperature information of each tank is output and displayed. The temperature sensor T1 of the inner vessel 1 also controls the steam valve or the electric heating pipe at the same time, so that the hot water in the inner vessel 1 is kept at a certain target temperature, e.g. 95 ℃. The temperature of the intermediate tank 2 and the outer tank 3 fluctuates, and the real-time actual temperature is displayed through the corresponding temperature sensors when the temperature sensor is used. The temperature sensors of the respective tanks, such as T in fig. 1, 2a, 2b, such as T1, T2, T3 in fig. 3. The number of the intermediate tanks can be one, or two or more. The water temperature between the plurality of intermediate tanks forms a gradient difference.
Furthermore, because the wall of the inner tank is the heat source of the intermediate tank, the wall of the intermediate tank is the heat source of the outer tank, only the outer wall of the outer tank 3 is the only radiating surface of the multilayer hot water storage tank, the surface temperature of the outer tank is lower, and a thick insulating layer b is arranged on the outer wall of the outer tank, so that the heat dissipation of the whole multilayer hot water storage tank is better prevented. Therefore, the heat dissipation of the multi-layer hot water storage tank of the present invention is very small.
Further, a first level sensor 8 is installed in the outer tank 3. When any tank of the multilayer hot water storage tank is drained, which causes the liquid level in each tank, including the outer tank 3, to drop to a certain extent, the first liquid level sensor 8 controls the water pump 112 to supply water to the outer tank 3 through the water inlet 9 on the outer wall, keeping the total water amount in the multilayer hot water storage tank constant. When the first liquid level sensor 8 detects that the liquid level returns to the original water level, the water pump 112 is controlled to stop working.
Further, the air in each tank is communicated, and the top of the outer tank 3 is provided with a vent pipe 10, so that the pressure in the tank caused by the water level change is eliminated.
As shown in fig. 3a, the utility model discloses still provide a heat recovery system of recycling for the heat energy that the heat absorption in-process produced is recycled, this system includes: a multi-story hot water storage tank, a collection water tank 11, and a heat absorption process unit 12 having a jacket a.
Wherein, the water outlet 5 of the multilayer hot water storage tank is communicated with the water inlet of the jacket a through a pipeline; the water outlet of the jacket a is communicated with the water inlet of the solar water heater 15. The water inlet of the solar water heater 15 can be externally connected with softened pipeline water. The water outlet of the solar water heater 15 is communicated with the water inlet of the water collecting tank 11 through a pipeline. The water outlet of the collecting water tank 11 is communicated with the water inlet 9 of the multilayer hot water storage tank through a pipeline.
In specific implementation, the water inlet of the solar water heater 15 may be externally connected with softened pipeline water, may be connected with the water outlet of the jacket of the heat absorption process equipment, or may be connected with both. The water inlet of the solar water heater 15 is externally connected with a water outlet of a softened pipe water and/or a jacket of heat absorption process equipment. The water outlet of the solar water heater 15 is communicated with the water collecting tank 11 through a pipeline.
The solar water heater 15 is communicated with the water collecting tank 11, mainly receives the recovered water from the jacket of the heat absorbing device, heats the recovered water and then flows into the water collecting tank 11. It also connects the demineralized line water. Normally, the softening conduit water valve is not opened, and the valve is opened when the water collecting tank 11 is short of water. The water collecting tank is provided with a second liquid level sensor 113, the second liquid level sensor 113 controls a water inlet pipeline valve of the solar water heater 15, and when the water level in the water collecting tank 11 is higher than a preset position, water inlet from a softened pipeline is stopped.
The collection tank 11 is provided with at least one water outlet, which may be one or more. A pump 112 is arranged between the water outlet of the collecting water tank and the water inlet 9 of the multilayer hot water storage tank, and the hot water recovered from each process is pumped into the multilayer hot water storage tank through the pump 112. The start or stop of the pump 112 is regulated by the first level sensor 8. The recovered water tank 11 is pumped by pump 112 to the multi-layered hot water storage tank through water inlet 9 into the outer tank 3.
The top of the collecting water tank 11 is provided with a vent/overflow port 111 to eliminate the pressure in the tank caused by the water level change, and overflow when the water level is too high, and overflow excessive recovered water.
The outer wall of the water collecting tank 11 is provided with a heat insulating layer, so that the heat energy of the water in the tank is not lost.
The utility model discloses among the heat recovery system of recycling, multilayer hot water storage tank is in the high-order, collects water tank 11 and is in the low level, and heat absorption process equipment 12 sets up at the intermediate position, and water can flow naturally, selects the temperature that needs through the valve, for example, the play water of each jar (inner tank, pans, outer jar) of high temperature steam or multilayer hot water storage tank to control hot water velocity of flow, play rivers flow to collect water tank 11.
Preferably, in the multi-layer hot water storage tank and the heat energy recycling system, all heat-involved equipment comprises a reaction kettle and a heat exchange layer, a hot water storage tank, a water collecting tank, a pipeline, a hot water connecting pipeline and the like arranged outside the reaction kettle, and heat insulation layers are arranged outside the reaction kettle and the kettle, so that the loss of heat energy is reduced. Since all of the water from the multi-story hot water storage tank is recycled to the collection tank and returned to the multi-story hot water storage tank by pump 112, only a small amount of water, which may be lost, needs to be replenished, which is controlled by the level sensor on the collection tank from the demineralized water supply. The amount of water collected in the water collection tank 11 depends on the amount of water used for all endothermic processes.
The solar water heater 15 increases the temperature of the recovered water fed into the water collecting tank 11 and the softened water in the pipeline to reduce the heating in the multi-layer hot water storage tank.
As shown in fig. 3b, the heat energy recycling system of the present invention further comprises: the heat-releasing process equipment 13 with a jacket a, the heat exchanger 14 and the preheating purified water storage tank 16 realize the recycling of heat energy generated in the heat-absorbing process and the recycling of heat energy generated in the heat-releasing process, and more comprehensively and fully recycle the heat energy generated in various heat-absorbing processes and heat-releasing processes in the production environment.
A water inlet of the jacket a is externally connected with clean water for production; the water outlet of the jacket a is communicated with the water inlet of the preheating purified water storage tank 16 through a pipeline. Specifically, if a lower temperature is required for the exothermic process device 13, cryogenic cooling water can be used to flow into jacket a of the exothermic process device 13. The cryogenic cooling water can be prepared by a refrigerator.
The heat exchanger 14 is a heat exchanger 14 for recovering heat energy of the high-temperature waste gas and waste water, the heat energy carried by the high-temperature waste gas and waste water in the production environment is transferred to water through heat exchange, the waste gas and waste water are converted into cold waste gas and waste water, and the water with the increased temperature flows into the preheating water purification storage tank 16, so that the heat energy is stored. The water inlet of the heat exchanger 14 is externally connected with clean water for production. The water outlet of the heat exchanger 14 is communicated with a preheating purified water storage tank 16 through a pipeline.
Specifically, when there is high-temperature exhaust gas or high-temperature waste water, clean water for production is turned on, heat exchange occurs at the heat exchanger 14, and the heat exchanger is turned off after use. The high-temperature exhaust gas and the high-temperature waste water transfer heat to the clean water for cold production in the heat exchanger 14, and after heat exchange, the water with increased temperature flows out of the heat exchanger 14 and flows into the collecting water tank 16 through a pipeline.
The utility model provides a heat recovery recycles method for recycle to the heat energy that takes place among the heat absorption process. Adopt the utility model discloses multilayer hot water storage tank and heat recovery system of recycling, it includes following step:
the water flows through the solar water heater 15 and flows into the water collecting tank 11;
pumping the water in the collecting water tank 11 into a water inlet 9 of the multilayer hot water storage tank by a pump 112;
the water flows through the solar water heater 15 and flows into the water collecting tank 11; pumping the water in the water collecting tank 11 into a water inlet 9 of the multilayer hot water storage tank by a pump 112, and enabling the water to enter the outer tank and enter the intermediate tank and the inner tank through a through hole 7;
regulating and controlling the temperature of the water in the inner tank 1 by heating the heating pipe 4;
according to different temperatures required by the heat absorption process equipment, selecting and selecting water with different temperatures, so that the water in the inner tank 1, the intermediate tank 2 and/or the outer tank 3 flows out from the water outlet 5 and flows into a jacket a of the heat absorption process equipment 12, after heat exchange, the water with reduced temperature flows out through the water outlet of the jacket a, then flows through the solar water heater 15 to be heated and flows into the water collection tank 11;
when the liquid level in the multilayer hot water storage tank drops, the pump 112 controlled by the first liquid level sensor 8 pumps water into the water inlet 9 of the multilayer hot water storage tank, and water enters the outer tank 3 and circulates between adjacent tanks through the through hole 7.
When the liquid level in the multilayer hot water storage tank drops, the pump 112 controlled by the first liquid level sensor 8 pumps the recovered water in the collected water tank 11 into the water inlet 9 of the multilayer hot water storage tank and enters the outer tank 3; the water amount in the outer tank 3 is increased, and water flows into the intermediate tank and the inner tank through the through holes 7, so that the liquid level in the multilayer hot water storage tank is lifted until the multilayer hot water storage tank returns to the original position; when the first liquid level sensor 8 detects that the liquid level returns to the original position, the regulating pump 112 stops working, and the water in the collecting water tank 11 is not pumped into the multilayer hot water storage tank any more;
the collected water tank 11 recovers the recovered water flowing out of the jacket a of the endothermic process device 12.
The multilayer hot water storage tank adopts a central heating mode, and the temperature of the water in the inner tank 1 is regulated and controlled through the heating pipe 4. Heat is gradually transferred from the inner tank to the intermediate tank and the outer tank. The inner tank, the intermediate tank and the outer tank are separated by a heat insulation layer, and the heat transfer speed and efficiency are limited to a certain extent by the heat insulation layer between the storage tanks, so that a stepped temperature difference of a certain extent is formed between the tanks, and preferably, a temperature difference of about 15-20 ℃ exists between the adjacent storage tanks.
According to the different temperatures needed by the heat absorption process equipment 12 and the heat absorption process equipment thereof, different valves can be selected for regulation, and hot water flows with different temperatures are respectively introduced from the inner tank 1, the intermediate tank 2 and/or the outer tank 3 of the multi-layer hot water storage tank. The water can be discharged from a single tank, or the mixed water can be discharged from two tanks simultaneously so as to meet the actual required temperature. The hot water flows out of the water outlet and then flows into the jacket a of the heat absorbing process device 12, and the heat of the water is absorbed by the heat absorbing process occurring in the heat absorbing process device.
Hot water enters the jacket a, and the whole heat absorption process equipment is regulated, controlled and kept in a stable and balanced heating state, so that the temperature of each part in the heat absorption process equipment is basically consistent, and the technical problem of excessive reaction or insufficient reaction caused by the condition that the temperature is too high or too low at the local position of the reaction in the prior art is solved.
As the heat absorbing process device proceeds and absorbs heat, the temperature of the water in the jacket a decreases after heat exchange. The water having the decreased temperature flows out through the water outlet of the jacket a and flows into the collection water tank 11.
Next, when the liquid level in the multi-story hot water storage tank drops, the pump 112 controlled by the first liquid level sensor 8 pumps the recovered water in the collection water tank 11 into the multi-story hot water storage tank. The above method is repeated cyclically.
In the heat energy recycling system and method, hot water with different temperatures provided by the multi-layer hot water storage tank provides a source of heat energy for endothermic reaction, and realizes the purpose of uniform heat supply to enable the reaction to be better, and the endothermic reaction is utilized to reduce the water temperature, and the hot water is recycled to the water collection tank 11 and is in a heat preservation state. When needed, the recovered water is supplemented into the multilayer hot water storage tank and circulates in the tank, and the hot water storage with stage temperature difference in each tank is formed under the regulation and control of central heating of the inner tank 1 and the arrangement of the heat insulation layer. According to different requirements of reaction temperature in the heat absorption process equipment, the valve switch is adjusted, and hot water meeting the requirements is introduced into the heat absorption process equipment. The circulation is carried out without consuming extra energy provided by the outside.
Further, the present invention also provides another method for recycling heat energy, which comprises recycling heat emitted from the heat-releasing process equipment 13. That is, softened pipeline water is injected into jacket a of the exothermic process device 13, and the chemical reaction occurring in the exothermic process device releases a large amount of thermal energy, which is absorbed by the water in jacket a, thereby raising the temperature of the water. The water with the increased temperature flows out from the water outlet of the jacket a and flows into the water collecting tank 11. When the liquid level in the multi-layered hot water storage tank drops, the recovered water in the collected water tank 11 is pumped into the multi-layered hot water storage tank by the pump 112 controlled by the liquid level sensor 8. The above method is repeated cyclically.
When a lower temperature water is required to flow into the jacket a, then a low temperature cooling water can be used. Cooling with low-temperature cooling water, and returning the effluent to the refrigerator.
The method comprises utilizing solar energy with a solar water heater 15. The water inlet of the solar water heater 15 is externally connected with softened pipeline water, the solar water heater 15 works to convert solar energy into water temperature to be increased and stored, the water with the increased temperature is conveyed to the water collecting tank 11 through the water outlet of the solar water heater 15 to be stored, and when the liquid level in the multilayer hot water storage tank is reduced, the pump 112 controlled by the first liquid level sensor 8 pumps the recovered water in the water collecting tank 11 into the multilayer hot water storage tank. The above method is repeated cyclically.
Preferably, the heating step is carried out by introducing water at a temperature higher than the desired temperature by 15 ℃ or more, or by taking water from two storage tanks simultaneously to reach the desired temperature.
Preferably, for the process to be cooled, water with temperature lower than the temperature to be cooled by less than 10 ℃ is selected, if the cooled water is steam, the steam is often provided with a large amount of vaporization heat, the tap water can be firstly used for condensing the steam into liquid in a heat exchanger, and then the cooling water is cooled to the required temperature.
The multilayer hot water storage tank is used as a heat source to replace the situation that only one energy source of steam (or electricity) is used for supplying different heat-requiring processes. Each of the heat-requiring devices selects the temperature of the input hot water according to the required temperature, and the water from the device flows into the collection water tank. The heat-requiring process is heated by steam (or electricity) when the temperature exceeds 100 ℃. The heat-requiring process can be various processes such as chemical reaction, traditional Chinese medicine extraction, concentration of water extract, distillation of organic solvent and the like.
The utility model recovers the heat released in different heat releasing processes, and introduces pipelines to cool the equipment in the system, and the hot water flows into the water collecting tank; or cooling with purified water, and flowing the hot water into a preheated purified water storage tank. The recovered waste heat can be generated by acid-base neutralization reaction, redox reaction, water decomposition reaction and other various reaction waste heat. The recovered waste heat may also be heat evolved by the liquefaction, cooling and solidification of the vapor. For hot waste gas and waste water generated in the production, the heat of cooling water of the equipment is recovered to a collecting tank or a preheating clean water storage tank through a heat exchanger.
When the temperature to be controlled is lower than the pipeline water, the pipeline water is cooled by low-temperature cooling water, and the hot water flows back to the refrigerator.
For plants without steam supply, an electrically heated multi-layer hot water storage tank can be adopted, and then a hot water jacket is used for heating to replace the direct electric heating of the equipment.
Example 1
Heating is an indispensable process in chemical plants and pharmaceutical factories, and stirring jacket steam is mostly adopted to heat a reaction kettle in the prior art. The heat transfer from the kettle wall to the reaction liquid is contact transfer, while the reaction liquid is stirred transfer, and actually, the temperature of the reaction liquid on the kettle wall and the temperature of the reaction liquid in the middle can be 7-8 ℃ different due to heat transfer. And tends to be much higher at the upper edge of the reaction liquid because the vapor temperature is too high, causing the local temperature of the wall of the vessel to be too high. Such temperature non-uniformity tends to adversely affect the reaction and reduce the quality and yield of the product. And utilize the utility model provides a scheme then can avoid aforementioned problem. The system and method of the present invention can be applied to extraction or reaction temperatures below 100 ℃. If the utility model discloses in, in the endothermic reaction process equipment 12, adopt and press from both sides cover a instant heating jacket heating, there is not the local overheated condition to take place, temperature control is more steady and accurate.
From the heat energy view: the steam is characterized by high heat, large volume and small mass; while hot water is much denser than steam. According to rough calculation, 1 cubic 120 ℃ steam contains evaporation heat which is equivalent to the heat released by cooling 1 cubic water by 10 ℃.
The electric heating is carried out, the temperature of 1 cubic meter of water is raised to 50 ℃, the energy is required to be 1000 multiplied by 4.184kJ/kg DEG C multiplied by 50 to 209200kJ, and if the energy is reached in half an hour, the power is required to be 116 kilowatts. However, if the water in the hot water tank of the system of the utility model is adopted, the same amount of energy can be input into the hot water tank within 24 hours and then be used in a centralized way. The theoretical electrical power required is only 1/48 kilowatts at 116 kilowatts, which results in a significant reduction in thermal power and thus a considerable reduction in investment from the heating apparatus.
Example 2
Concentration of aqueous solutions in traditional chinese medicine plants and chemical plants is the most common process, such as multiple effect evaporators. However, some chemical components are unstable, so that the heating at high temperature for a long time is not suitable, the heating temperature by pressure steam is difficult to control, and the product quality cannot be guaranteed. Adopt the utility model discloses recovery system can solve this problem. If these components can withstand 65 ℃, reduced pressure distillation can be used, and since the boiling point of water is 65 ℃ under 25kPa, a WLW-50 vacuum pump can be used in a general water distillation process, the vacuum degree is reduced to below 25kPa, and the water is heated to 65 ℃ or higher by selecting appropriate hot water, and the discharged water is passed into the collection water tank 11. Thus, no pressure steam is necessary. If the chemical components are less temperature resistant, they can be concentrated by increasing the vacuum, or water at a lower temperature, but at a slower rate, can be used for heating.
Example 3
The extraction is a purification process commonly used in chemical and pharmaceutical factories, and organic solvents in the extraction comprise: halogenated hydrocarbons such as chloroform, dichloromethane and the like, aromatic hydrocarbons such as benzene and the like, aliphatic hydrocarbons such as kerosene, petroleum ether and the like, esters such as butyl acetate, ethyl acetate and the like. The solvent of the organic phase after extraction is distilled off, and the distillation process of the solvent with the boiling point lower than 100 ℃ can be used by the heat energy recycling system and the method. In the case of dichloromethane, after extraction, the dichloromethane is distilled off, the boiling point is 39.75 ℃, and the distillation can be carried out by heating with water at 50-60 ℃, for example, with hot water from the outer tank 3, and with water at a higher temperature in the last stage when the solution is very concentrated, for example, with hot water from the intermediate tank 2.
Water from the jacket in the endothermic process device 12 can be returned to the catch tank 11. While the methylene chloride is collected in the condenser of the exothermic process device 13, the cooling water flowing into the jacket a of the condenser is cooled with low-temperature cooling water, and the temperature of the discharged water is still lower than that of tap water and can be returned to the refrigerator.
Example 4
Acid-base neutralization is also a common process in chemical plants involving inorganic acidic and basic compounds, organic acids and organic bases, releasing a large amount of heat, which is lost without prior art recovery. The acid and the alkali neutralize to generate water, the enthalpy of generation is-286 kJ/mol, 1 kilogram of water is generated, the heat is released by 15889 kilojoules, the temperature of 76 kilograms of water can be raised by 50 ℃, and the recoverable heat can be seen to be considerable. Temperature control in the acid-base neutralization reaction, slow reaction utilize the utility model discloses system and method, acid-base neutralization reaction go on in exothermic reaction process equipment 13's reation kettle, pour into the cover that presss from both sides of exothermic process equipment 13 with demineralized pipe water, the heat energy of release transmits to the water that presss from both sides in the cover a in the exothermic reaction, makes its temperature rise, and the water that flows out in this cover that presss from both sides passes through the pipeline and transmits the collection water tank 11. The heat energy released in the exothermic reaction is stored in a warm water mode in the collecting water tank 11 for recycling in the system of the utility model.
In addition to acid-base neutralization, there are many other exothermic reactions in chemical plants, such as redox reactions, water-splitting reactions, and the like. The large amount of heat evolved by the reaction can also be recovered. The cooling water is usually discharged. If cooled with water, the effluent can be sent to a collection tank.
The protection of the present invention is not limited to the above embodiments. Variations and advantages that may occur to those skilled in the art may be incorporated into the invention without departing from the spirit and scope of the inventive concept, and the scope of the appended claims is intended to be protected.
Claims (10)
1. A multi-layered hot water storage tank, comprising: the inner tank (1), at least one intermediate tank (2) and the outer tank (3) are sequentially nested from inside to outside; wherein,
a heating pipe (4) is arranged in the center of the inner tank (1);
the bottoms of the inner tank (1), the intermediate tank (2) and the outer tank (3) are respectively provided with a water outlet (5); a water inlet (9) is formed in the outer wall of the outer tank (3);
the tank walls of the inner tank (1) and the intermediate tank (2) are respectively provided with at least one through hole (7);
the inner tank (1), the intermediate tank (2) and the outer tank (3) are respectively provided with a temperature sensor (T);
the tank walls of the inner tank (1), the intermediate tank (2) and the outer tank (3) are heat insulation layers (6).
2. Multilayer hot water storage tank according to claim 1, characterized in that further the outer tank (3) is provided with a first level sensor (8); the top of the outer tank (3) is provided with a vent pipe (10); and the outer wall of the outer tank (3) is provided with a heat-insulating layer.
3. Multilayer hot water storage tank according to claim 1, characterized in that the inner tank (1), the intermediate tank (2) and the outer tank (3) are cylindrical, cubic, spherical.
4. The multilayer hot water storage tank as claimed in claim 1, wherein the temperature difference of water between the adjacent inner tank (1) and the intermediate tank (2) is 15-20 ℃; the temperature difference of water between the adjacent intermediate tanks (2) and the intermediate tank (2) is 15-20 ℃; the temperature difference of water between the adjacent intermediate tank (2) and the outer tank (3) is 15-20 ℃; the water temperature of the inner tank (1) is 95 ℃, the water temperature of the intermediate tank (2) is 75-80 ℃, and the water temperature of the outer tank (3) is 55-65 ℃.
5. Multilayer hot water storage tank according to claim 1, characterized in that the inner tank (1), the intermediate tank (2) and the outer tank (3) are of a multilayer arrangement or of a multilayer jacketed arrangement.
6. A thermal energy recovery and reuse system, comprising: the multi-layered hot water storage tank, the collection water tank (11), the endothermic process device (12) with jacket (a), and the solar water heater (15) according to claim 1;
wherein, the water outlet (5) of the multilayer hot water storage tank is communicated with the water inlet of the jacket (a) through a pipeline;
the water outlet of the jacket (a) is communicated with the water inlet of the solar water heater (15) through a pipeline;
a water inlet of the solar water heater (15) is externally connected with softened pipeline water; the water outlet of the solar water heater (15) is communicated with the water collecting tank (11) through a pipeline;
the water outlet of the collecting water tank (11) is communicated with the water inlet (9) of the multilayer hot water storage tank through a pipeline; a pump (112) is arranged between the water outlet of the collecting water tank (11) and the water inlet (9).
7. The thermal energy recovery and reuse system according to claim 6, characterized in that said collection water tank (11) is provided with a vent/overflow (111), a second level sensor (113).
8. The heat energy recovery and reuse system according to claim 6, characterized in that the collection water tank (11) is provided with an insulation layer.
9. The heat energy recovery and reuse system according to claim 6, further comprising an exothermic process device (13) having a jacket (a), a heat exchanger (14), a preheated clean water storage tank (16);
the preheating purified water storage tank (16) is provided with at least one water inlet and at least one water outlet;
a water inlet of a jacket (a) of the heat release process equipment (13) is externally connected with production pure water; the water outlet of the jacket (a) is communicated with the water inlet of the preheating purified water storage tank (16) through a pipeline;
a water inlet of the heat exchanger (14) is externally connected with production purified water; the water outlet of the heat exchanger (14) is communicated with the preheating purified water storage tank (16) through a pipeline;
the water outlet of the preheating purified water storage tank (16) is communicated to the heat absorption process equipment (12) or the solar water heater (15) through a pipeline.
10. The heat energy recovery and reuse system according to claim 9, wherein the preheated clean water tank (16) is provided with a third level sensor (161), a vent/overflow (162), and an insulation layer.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110422955A (en) * | 2019-08-27 | 2019-11-08 | 齐鲁工业大学 | A kind of recycling reuse method carrying out dangerization spent acid using reaction heat |
| CN110470051A (en) * | 2018-05-09 | 2019-11-19 | 上海科德实业有限公司 | A kind of multilayer hot water storage tank, thermal energy recycling and reusing system and its reuse method |
| CN114484867A (en) * | 2022-01-25 | 2022-05-13 | 爱能森（深圳）高端智能装备有限公司 | Industrial waste heat type ultra-high temperature heat pump unit |
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2018
- 2018-05-09 CN CN201820685158.0U patent/CN208349557U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110470051A (en) * | 2018-05-09 | 2019-11-19 | 上海科德实业有限公司 | A kind of multilayer hot water storage tank, thermal energy recycling and reusing system and its reuse method |
| CN110422955A (en) * | 2019-08-27 | 2019-11-08 | 齐鲁工业大学 | A kind of recycling reuse method carrying out dangerization spent acid using reaction heat |
| CN114484867A (en) * | 2022-01-25 | 2022-05-13 | 爱能森（深圳）高端智能装备有限公司 | Industrial waste heat type ultra-high temperature heat pump unit |
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