CN109813166A - The energy recycling system and control method of sewage - Google Patents

The energy recycling system and control method of sewage Download PDF

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Publication number
CN109813166A
CN109813166A CN201910063650.3A CN201910063650A CN109813166A CN 109813166 A CN109813166 A CN 109813166A CN 201910063650 A CN201910063650 A CN 201910063650A CN 109813166 A CN109813166 A CN 109813166A
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China
Prior art keywords
sewage
process water
trade effluent
recycling system
pump
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CN201910063650.3A
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Chinese (zh)
Inventor
王珏
周明冬
梁枫
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Xinao Shuneng Technology Co Ltd
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Xinao Shuneng Technology Co Ltd
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Priority to CN201910063650.3A priority Critical patent/CN109813166A/en
Publication of CN109813166A publication Critical patent/CN109813166A/en
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Abstract

The invention discloses a kind of energy recycling system of sewage and its control methods, the energy recycling system of sewage includes sewage draw-out device, heat-exchanger rig and controller, trade effluent for extracting high-temperature, heat-exchanger rig includes the first access and alternate path, first access is for flowing through trade effluent, alternate path is used to flow through the process water of low temperature, wherein, heat-exchanger rig is used to carry out heat exchange to trade effluent and process water, to utilize the thermal energy of process water recycling trade effluent, controller is connected with sewage draw-out device, to control the sewage extraction amount of sewage draw-out device, adjust the heat exchange efficiency of heat-exchanger rig.The energy recycling system of sewage according to the present invention, trade effluent can carry out high efficient heat exchanging to process water, without separately heating to process water, save the energy.

Description

The energy recycling system and control method of sewage
Technical field
The present invention relates to heat exchange control fields, in particular to the energy recycling system and control method of a kind of sewage.
Background technique
In the related technology, in production operation, the sewage temperature of sewage discharge is very high, and even as high as 87-88 DEG C, if sewage It is directly entered cesspool, will cause the very big waste of sewerage heat energy, and influence the processing of sewage plant.In addition, in dyeing, rinsing etc. Higher with coolant-temperature gage in production technology, industrial water needs additional heating, needs to expend compared with large resource.In addition, sewage discharge system System controls sewage discharge by the way of manual control water pump pump pressure, not can guarantee and timely responds to the variation of blowdown operating condition, Functional reliability is poor.
Summary of the invention
The present invention is directed to solve at least some of the technical problems in related technologies.For this purpose, of the invention First aspect proposes a kind of energy regenerating system of sewage that at least to a certain extent can be energy saving and high functional reliability System.
The second aspect of the present invention proposes a kind of control method of the energy recycling system of sewage.
The third aspect of the present invention proposes a kind of non-transitory readable storage medium storing program for executing.
The fourth aspect of the present invention proposes a kind of apparatus for energy recovery of sewage.
The energy recycling system of the sewage according to a first aspect of the present invention, including sewage draw-out device, heat-exchanger rig And controller, the sewage draw-out device are used for the trade effluent of extracting high-temperature, the heat-exchanger rig includes the first access and the Two accesses, first access are used to flow through the process water of low temperature for flowing through the trade effluent, the alternate path, In, the heat-exchanger rig is used to carry out heat exchange to the trade effluent and the process water, to utilize the process water The thermal energy of the trade effluent is recycled, the controller is connected with the sewage draw-out device, extracts dress to control the sewage The sewage extraction amount set, adjusts the heat exchange efficiency of the heat-exchanger rig.
The energy recycling system of the sewage, trade effluent can carry out process water according to a first aspect of the present invention High efficient heat exchanging has saved the energy without separately heating to process water.
Further, the sewage draw-out device includes filter and sewage pump, and the filter is for filtering the work The impurity of industry sewage, the upstream of the filter are equipped with sewage transfer puddle, and the sewage pump is used for from the sewage transfer water It extracts sewage and flow to the heat-exchanger rig after filtering via the filter in hole.
Further, the controller is used for according in the water level, flow velocity, temperature and pressure in sewage transfer puddle At least one adjusts the pump pressure of the sewage pump.
Further, sewage transfer puddle is equipped with overflow ducts, and the overflow ducts are connected with cesspool, in institute When stating the water level in sewage transfer puddle and reaching the overflow ducts, trade effluent is discharged into the cesspool automatically.
Further, the energy recycling system further includes process water water pump, flows through the alternate path to adjust The flow of process water, wherein the process water water pump is controlled by the controller.
The control method of the energy recycling system of sewage according to a second aspect of the present invention, comprising the following steps:
Receive control signal;
According to the trade effluent of the control signal extraction high temperature, to carry out hot friendship to the trade effluent and process water It changes, the thermal energy of the trade effluent is recycled using the process water.
The control method of the energy recycling system of the sewage according to a second aspect of the present invention, trade effluent can be to work Skill carries out high efficient heat exchanging with water, without separately heating to process water, has saved the energy.
Further, the trade effluent according to the control signal extraction high temperature, comprising:
Detect at least one of the water level, flow velocity, temperature and pressure of trade effluent;
At least one of water level, flow velocity, temperature and pressure according to the trade effluent adjust the trade effluent Extraction amount.
Further, the control method further include:
The flow of process water is adjusted, to adjust the efficiency that the process water recycles the thermal energy of the trade effluent.
Non-transitory readable storage medium storing program for executing according to a third aspect of the present invention is stored thereon with computer program, the meter The control method of the energy recycling system of sewage described in second aspect of the present invention is realized when calculation machine program is executed by processor.
The non-transitory readable storage medium storing program for executing according to a third aspect of the present invention, trade effluent can to process water into Row high efficient heat exchanging has saved the energy without separately heating to process water.
The apparatus for energy recovery of sewage according to a fourth aspect of the present invention, including memory, processor and it is stored in storage On device and the energy recovery procedure of sewage that can run on a processor, the processor execute the energy regenerating journey of the sewage The control method of the energy recycling system of sewage described in second aspect of the present invention is realized when sequence.
The apparatus for energy recovery of the sewage, trade effluent can carry out process water according to a fourth aspect of the present invention High efficient heat exchanging has saved the energy without separately heating to process water.
Additional aspect and advantage of the invention will be set forth in part in the description, and will partially become from the following description Obviously, or practice through the invention is recognized.
Detailed description of the invention
Above-mentioned and/or additional aspect of the invention and advantage will become from the description of the embodiment in conjunction with the following figures Obviously and it is readily appreciated that, in which:
Fig. 1 is the structural schematic diagram of the apparatus for energy recovery of the sewage of the embodiment of the present invention;
Fig. 2 is the flow chart of the control method of the energy recycling system of the sewage of the embodiment of the present invention.
Appended drawing reference:
Energy recycling system 100, sewage transfer puddle 1, cesspool hygrosensor 10, sewage intake line 11, first Access 12, the first common pipeline 121, the first spare duct 122, the second common pipeline 123, the second spare duct 124, overflow are logical Road 13, sewage pump 14 commonly use sewage pump 141, spare sewage pump 142, sewage flowmeter 15, sewage temperature detector 16, sewage Pressure detector 17, filter 18, flush loop 181, water-level gauge 19, heat-exchanger rig 2, process water pond 3, process water pond temperature Detector 30 is spent, process water output pipe 31, alternate path 32, process water pump 33, process water flowmeter 34, technique is used Coolant-temperature gage detector 35, process water pressure detector 36, sewage treatment terminal 41, process water terminal 42, the manufacturing side 43, control Device 5 processed, cesspool 6.
Specific embodiment
The embodiment of the present invention is described below in detail, examples of the embodiments are shown in the accompanying drawings, wherein from beginning to end Same or similar label indicates same or similar element or element with the same or similar functions.Below with reference to attached The embodiment of figure description is exemplary, it is intended to is used to explain the present invention, and is not considered as limiting the invention.
In the present invention unless specifically defined or limited otherwise, term " installation ", " connected ", " connection ", " fixation " etc. Term shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integral;It can be mechanical connect It connects, is also possible to be electrically connected or can communicate with each other;It can be directly connected, can also indirectly connected through an intermediary, it can To be the interaction relationship of connection or two elements inside two elements.For the ordinary skill in the art, The specific meanings of the above terms in the present invention can be understood according to specific conditions.
With reference to the accompanying drawing and with reference to the specific embodiment description present invention.
Fig. 1 is combined to describe the energy recycling system 100 of the embodiment of the present invention first.
As shown in Figure 1, the energy recycling system 100 of the embodiment of the present invention may include that sewage draw-out device (such as filters Device and sewage pump etc.), heat-exchanger rig 2 and controller 5.Sewage draw-out device is used for the trade effluent of extracting high-temperature, heat-exchanger rig 2 Including the first access 12 and alternate path 32, the first access 12 is for flowing through trade effluent, and alternate path 32 is for flowing through low temperature Process water, wherein heat-exchanger rig 2 is used to carry out heat exchange to trade effluent and process water, to be returned using process water The thermal energy of trade effluent is received, controller 5 is connected with sewage draw-out device, to control the sewage extraction amount of sewage draw-out device, adjusts Save the heat exchange efficiency of heat-exchanger rig.It is possible thereby to guarantee that the extraction amount of trade effluent is corresponding with process water consumption to be exchanged heat, with Keep target process hydro-thermal magnitude equal with sewerage heat energy value, makes the heat exchange efficiency highest between trade effluent and process water.
Trade effluent can carry out high efficient heat exchanging to process water as a result, without separately heating to process water, save energy Source.
Specifically, sewage draw-out device includes filter 18 and sewage pump 14, and filter 18 is for filtering trade effluent Impurity, the upstream of filter 18 are equipped with sewage transfer puddle 1, and sewage transfer puddle 1 is connected with sewage intake line 11 and the The sewage of one access 12, the manufacturing side 43 (such as the production lines such as dyeing, rinsing) discharge can be flowed by sewage intake line 11 Sewage transfer puddle 1 temporarily stores, and the first access 12 can be by the sewage in sewage transfer puddle 1 by transporting after heat-exchanger rig 2 Sewage treatment is carried out to sewage treatment terminal 41 (such as sewage treatment plant).
Filter 18 is passing through filter 18 for the impurity (such as the impurity such as fine, soft fur, sandstone) in filter sewage, sewage Enter heat-exchanger rig 2 after filtering, avoids exchange thermal 2 from damaging with the impurity in sewage.In some instances, filter 18 can be basket filter, bag type filter or fixed net type filter.
Specifically, controller 5 is used at least one of water level, flow velocity, temperature and pressure according to sewage transfer puddle 1 Adjust the pump pressure of sewage pump 14.For example, controller can wastewater level in sewage transfer puddle 1 is higher or sewage pressure compared with When greatly or effluent flow rate is very fast, trade effluent can be discharged in time from sewage transfer puddle 1, avoided in sewage transfer puddle 1 Sewage overflow.Controller can trade effluent temperature in sewage transfer puddle 1 it is higher when, can be by the industry of less flow Sewage is discharged from sewage transfer puddle 1, to avoid the heat waste of trade effluent, improves heat exchange property.
As shown in Figure 1, storing the water for production in process water pond 3, it is defeated that process water pond 3 is connected with process water Pipeline 31 and alternate path 32 out, alternate path 32 can be by the process waters for being used to produce in process water pond 3 by changing Process water pond 3 is flowed back to after thermal 2 and sewage heat change.Such as between process water can be carried out by heat-exchanger rig 2 and sewage Connect heating so that the process water in process water pond 3 have suitable temperature, therefore without additionally to process water heat, The energy is saved.When the process water temperature in process water pond 3 reaches production requirement, process water output pipe 31 can be with The process water in process water pond 3 is transported to process water terminal 42 (such as the production lines such as dyeing, rinsing).
Wherein, the first access 12 is connected with sewage pump 14, and sewage pump 14 is for driving the sewage in sewage transfer puddle 1 to pass through First access 12 flows to and is equipped with water-level gauge 19 in sewage transfer puddle 1, and sewage pump 14 is suitable for according in sewage transfer puddle 1 The highly automated start and stop of wastewater level.Wastewater level height is greater than or equal to the lowest water level in sewage transfer puddle 1 constantly, sewage pump 14 open, and wastewater level height is lower than the lowest water level in sewage transfer puddle 1 constantly, and sewage pump 14 is closed, to prevent in sewage The sewage for turning puddle 1 is very few and cannot be introduced into the first access 12 causes sewage pump 14 to dally, to save resource.It is dirty as a result, Water pump 14, which can change blowdown operating condition, to be timely responded to, and functional reliability is high.
In some optional embodiments of the invention, as shown in Figure 1, between sewage treatment terminal 41 and heat-exchanger rig 2 It is connected with cesspool 6, cooling sewage can be summarized after heat exchange with temporary flow to cesspool 6, and cesspool 6 is suitable for summarizing more The sewage of multiple energy recycling systems 100 can be emitted into dirt in concentration by the sewage in a sewage transfer puddle 1, i.e. cesspool 6 Behind pond 6, sewage treatment terminal 41, the long range pipe of cesspool 6 and sewage treatment terminal 41 are being emitted into from the concentration of cesspool 6 Road arrangement is simpler, has saved cost.
Specifically, as shown in Figure 1, sewage transfer puddle 1 is equipped with overflow ducts 13, the sewage in sewage transfer puddle 1 is suitable for Cesspool 6 is flowed by overflow ducts 13 when water level in sewage transfer puddle 1 is excessively high.In some specific examples, overflow The position that channel 13 is connected to sewage transfer puddle 1 is in the height in sewage transfer puddle 1 and the flood stage in sewage transfer puddle 1 It is highly identical, when so that the water level in sewage transfer puddle 1 is excessively high and reaching flood stage, the moisture storage capacity in sewage transfer puddle 1 It can no longer meet demand, sewage transfer puddle 1 will overflow, and the sewage in the puddle of sewage transfer at this time 1 can be in time by overflowing Circulation road 13 flows into cesspool 6, to keep sewage discharge process more reliable.
Specifically, as shown in Figure 1, alternate path 32, which is equipped with process water, pumps 33, process water flowmeter 34, process water Hygrosensor 35 and process water pressure detector 36, process water pump 33 is for driving the process water in process water pond 3 In 32 internal circulation flow of alternate path, process water flowmeter 34 is used to measure the process water flow in alternate path 32, work Skill is located at the downstream of heat-exchanger rig 2 with coolant-temperature gage detector 35 in alternate path 32, and process water hygrosensor 35 is used for The process water temperature before the process water in alternate path 32 heats up by heat-exchanger rig 2 is measured, process water pressure is visited It surveys device 36 and is used to measure the driving pressure in alternate path 32, i.e. process water pump pump pressure.Process water pond 3 is equipped with for measuring The process water pond hygrosensor 30 of process water temperature in process water pond 3.
As shown in Figure 1, the first access 12 is equipped with sewage flowmeter 15, sewage temperature detector 16 and sewage pressure detector 17, sewage flowmeter 15 is used to measure the discharge of sewage in the first access 12, and sewage temperature detector 16 is in the first access 12 Positioned at the downstream of heat-exchanger rig 2, the sewage that sewage temperature detector 16 is used to measure in the first access 12 is dropped by heat-exchanger rig 2 Sewage temperature after temperature, sewage pressure detector 17 are used to measure the driving pressure in the first access 12, i.e. sewage pump is pumped. Sewage transfer puddle 1 is equipped with the cesspool hygrosensor 10 for measuring the sewage temperature in sewage transfer puddle 1.
As shown in Figure 1, controller 5 respectively with cesspool hygrosensor 10, process water pond hygrosensor 30, technique With water pump 33, process water flowmeter 34, process water hygrosensor 35, process water pressure detector 36, sewage pump 14, Sewage flowmeter 15, sewage temperature detector 16 and sewage pressure detector 17 connect.Controller 5 can be according to technique as a result, With process water circulation line temperature before pond temperature, heat exchange, the process water pump pump pressure of alternate path 32, alternate path 32 Sewage output pipe temperature, the first access 12 after at least one numerical value and cesspool temperature, heat exchange in process water flow Sewage pump pump pressure, the first access 12 the discharge of sewage at least one numerical value, adjust sewage pump 14 and/or process water pump 33 Pump pressure so that process water pond temperature, process water pump pump pressure, process water flow, cesspool temperature, sewage pump be pumped, At least one of sewage output pipe temperature meets life after process water circulation line temperature, heat exchange before the discharge of sewage, heat exchange Production and emissions requirements.
More specifically, energy recycling system 100 further includes display, display respectively with cesspool hygrosensor 10, process water pond hygrosensor 30, process water flowmeter 34, process water hygrosensor 35, process water pressure Detector 36, sewage flowmeter 15, sewage temperature detector 16 and sewage pressure detector 17 connect, so that display can be shown Show process water circulation line temperature before process water pond temperature, heat exchange, process water pump pump pressure, process water flow and dirt Sewage output pipe temperature, sewage pump pump pressure, the discharge of sewage after pond temperature, heat exchange.
Personnel can monitor the process water in the real-time process water pond 3 of energy recycling system 100 by display as a result, Temperature, the process water temperature of alternate path 32, process water pump pump pressure, process water flow and sewage transfer puddle 1 Sewage temperature, the sewage temperature of the first access 12, sewage pump pump pressure, the discharge of sewage, in 100 operation irregularity of energy recycling system (process water circulation line temperature, process water pond temperature, process water pump pump pressure, process water flow, heat exchange before exchanging heat At least one of sewage output pipe temperature, cesspool temperature, sewage pump pump pressure, discharge of sewage occur abnormal afterwards), and control When device 5 controls abnormal (such as process water circulation line temperature, process water pond temperature, process water pump pump pressure, work before exchanging heat Sewage output pipe temperature, cesspool temperature, sewage pump pump pressure, the discharge of sewage for a long time can not be extensive after skill water flow, heat exchange It is multiple normal), it can find and take measures in time, to be further ensured that the functional reliability of energy recycling system 100.
Specifically, controller 5 is computer.
Specifically, as shown in Figure 1, the first access 12 is equipped with the first common pipeline 121, the first spare duct 122, second often With pipeline 123 and the second spare duct 124, sewage pump 14 includes common sewage pump 141 and spare sewage pump 142.
Wherein, it commonly uses sewage pump 141 to be located in the first common pipeline 121, spare sewage pump 142 is located at the first spare duct In 122, the first common pipeline 121 is in parallel with the first spare duct 122.Under normal circumstances, spare sewage pump 142, which is in, closes shape State is commonly used sewage pump 141 and is opened, and sewage is flowed by the common driving of sewage pump 141 in the first access 12.When common sewage pump When 141 damages or the first common blocking of pipeline 121 or the first common pipeline 121 overhaul, spare sewage pump 142 can be opened Driving sewage is flowed in the first access 12.
In some instances, as shown in Figure 1, controller 5 can carry out common sewage pump 141 and spare sewage pump 142 Control.In other examples, controller 5 can be controlled common sewage pump 141, and spare sewage pump 142 can be manual It opens, with when controller 5 and common sewage pump 141 fail, manually opened spare sewage pump 142 carries out emergency drainage.
Second common pipeline 123 is in parallel with the second spare duct 124, after the second common pipeline 123 is connect with heat-exchanger rig 2 It is connect with sewage treatment terminal 41, the second spare duct 124 does not connect with heat-exchanger rig 2 and directly connects with sewage treatment terminal 41 It connects.Under normal circumstances, the second spare duct 124 is in close state, and the second common pipeline 123 is opened, the common pipe of sewage second Sewage treatment terminal 41 is flow to after road 123 and process water heat exchange.When the second common blocking of pipeline 123 or the second common pipeline When 123 maintenance or process water are without heat exchange demand, the second common pipeline 123 can be made to be in close state, the second spare pipe Road 124 is opened, and sewage directly passes through the second spare duct 124 and flow to sewage treatment terminal 41.
The control method of the energy recycling system 100 of the embodiment of the present invention is described below with reference to Fig. 1-Fig. 2.
As Figure 1-Figure 2, the control method of the energy recycling system 100 of the embodiment of the present invention includes:
Step 101, control signal is received.For example, controller 5 receives control signal.
Step 102, according to the trade effluent of control signal extraction high temperature, to carry out hot friendship to trade effluent and process water It changes, utilizes the thermal energy of process water recycling trade effluent.For example, controller 5, which controls sewage draw-out device, extracts trade effluent, and Heat exchange is carried out with process water.
Control method according to an embodiment of the present invention, trade effluent can carry out high efficient heat exchanging to process water, without another Process water is heated, the energy has been saved.
Specifically, in step 102, according to the trade effluent of control signal extraction high temperature, comprising:
Detect at least one of the water level, flow velocity, temperature and pressure of trade effluent;
The extraction amount of at least one of water level, flow velocity, temperature and pressure according to trade effluent adjusting trade effluent.
Specifically, control method further include:
The flow of process water is adjusted, to adjust the efficiency of the thermal energy of process water recycling trade effluent.
In some specific embodiments, controller 5 obtains process water circulation line temperature before process water flow, heat exchange Sewage output pipe temperature, cesspool temperature after degree, heat exchange.For example, process water flowmeter 34 measures the work of alternate path 32 After skill water flow, process water flow value can be transferred to controller 5.Sewage temperature detector 16 measures the first access 12 After sewage temperature after heat exchanger, sewage output pipe temperature after heat exchange can be transferred to controller 5.Process water temperature Degree detector 35 measures alternate path 32 after the process water temperature before heat exchanger, process water circulation before can exchanging heat Line temperature is transferred to controller 5.After cesspool hygrosensor 10 measures the sewage temperature in sewage transfer puddle 1, it can incite somebody to action Cesspool temperature is transferred to controller 5.
Controller 5, which subtracts each other target process pond temperature and the preceding process water circulation line temperature that exchanges heat, obtains target work Skill water temperature difference, target process are to reach the process water temperature of the production requirement of process water terminal 42, mesh with pond temperature Mark process water pond temperature can be set in advance in controller 5.Sewage output pipe temperature and sewage after controller 5 will exchange heat Pond temperature, which is subtracted each other, obtains the sewage temperature difference.
Controller 5 obtains the sewerage heat energy value of the first access 12 according to the sewage temperature difference, the discharge of sewage, and controller 5 is according to dirt Hydro-thermal magnitude obtains and the equal-sized target process hydro-thermal magnitude of sewerage heat energy value, i.e. target process hydro-thermal magnitude and dirt Hydro-thermal magnitude is equal, and the heat exchange efficiency of sewage and process water is maximum at this time.Controller 5 according to target process with hydro-thermal magnitude with And target process can go out target process water flow with water temperature difference with reverse.
Controller 5 changes the pump pressure of process water pump 33 according to target process water flow, it is possible thereby to make sewage and work Skill is maximum by the heat exchange efficiency of heat-exchanger rig 2 with water.
Specifically, as shown in Figure 1, sewage pressure detector 17 is located at the downstream of filter 18, mistake in the first access 12 Filter 18 is connected with flush loop 181, waterpower adjustment method further include:
Controller 5 obtains sewage pump pump pressure.For example, sewage pressure detector 17 measures the sewage pump pump pressure of the first access 12 Afterwards, sewage pump can be pumped and is transferred to controller 5.
When controller 5 judges that sewage pump pump pressure is greater than predetermined maximum sewage pump pressure safety value, the first access 12 at this time Hypertonia, the first access 12 are easy to appear risk of rupture, and therefore, the pump pressure that controller 5 controls sewage pump 14 declines and is equal to Predetermined maximum sewage is pumped safety value.Wherein, making a reservation for maximum sewage pump pressure safety value is the highest for preventing the first access 12 from rupturing Pressure, predetermined maximum sewage pump pressure safety value can be preset in the controller 5.
When controller 5 judges that sewage pump pump pressure is less than predetermined minimum sewage pump pressure value, illustrate that filter 18 may at this time Blocking occurs and causes most of sewage can not be by sewage pressure detector 17, controller 5 opens 181 pairs of flush loop filterings Device 18 is rinsed, and the impurity in filter 18 is washed out, and guarantees sewage smooth outflow in the first access 12.Predetermined minimum Sewage pump pressure value can be preset in the controller 5.
Further, waterpower adjustment method further include:
Controller 5 obtains process water pump pump pressure.For example, process water pressure detector 36 measures the work of alternate path 32 After skill is pumped with water pump, process water can be pumped into pump pressure and be transferred to controller 5.
When controller 5 judges that process water pump pump pressure is greater than predetermined maximum 33 pressure safety value of process water pump, at this time the The hypertonia of two accesses 32, alternate path 32 are easy to appear risk of rupture, and therefore, controller 5 controls process water pump 33 Pump pressure, which drops to, is equal to predetermined 33 pressure safety value of maximum process water pump.Wherein, make a reservation for maximum 33 pressure safety value of process water pump For the maximum pressure for preventing alternate path 32 from rupturing, predetermined 33 pressure safety value of maximum process water pump can be set in advance in control In device 5.
Specifically, waterpower adjustment method further include:
Controller 5 obtains the wastewater level height in sewage transfer puddle 1.For example, process water position meter 19 measures sewage After the wastewater level height in transfer puddle 1, the wastewater level height in sewage transfer puddle 1 can be transferred to controller 5.
Predetermined water level height is to guarantee minimum of the row in sewage transfer puddle 1 with sufficient amount to sewage treatment terminal 41 Volume, predetermined water level height can be preset in the controller 5.When controller 5 judges that wastewater level height is greater than or equal to When predetermined water level height, illustrate that the sewage in the puddle of sewage transfer at this time 1 passes through 12 row of the first access to sewage treatment terminal enough 41, controller 5 controls sewage pump 14 and opens.
When controller 5 judges wastewater level height lower than predetermined water level height, illustrate the dirt in the puddle of sewage transfer at this time 1 Water is not enough to through 12 row of the first access to sewage treatment terminal 41, and controller 5 controls sewage pump 14 and closes, to prevent sewage pump 14 idle running, save energy consumption.
The invention also provides a kind of non-transitorycomputer readable storage medium, non-transitory computer-readable storage mediums It is stored with computer program in matter, the sewage of any of the above-described kind of embodiment introduction is realized when computer program is executed by processor The control method of energy recycling system.
The invention also provides a kind of apparatus for energy recovery of sewage, including memory, processor and it is stored in memory The energy recovery procedure of sewage that is upper and can running on a processor, processor are realized when executing the energy recovery procedure of sewage Invent the control method of the energy recycling system of the sewage of any of the above-described kind of embodiment.
The apparatus for energy recovery of sewage according to the present invention, trade effluent can carry out high efficient heat exchanging, nothing to process water It needs separately to heat process water, has saved the energy.
Specifically, processor may be a central processing unit (Central Processing Unit, referred to as CPU), Either specific integrated circuit (Application Specific Integrated Circuit, referred to as ASIC), either It is configured to implement one or more integrated circuits of the embodiment of the present invention.
In the description of this specification, reference term " one embodiment ", " some embodiments ", " example ", " specifically show The description of example " or " some examples " etc. means specific features, structure, material or spy described in conjunction with this embodiment or example Point is included at least one embodiment or example of the invention.In the present specification, schematic expression of the above terms are not It must be directed to identical embodiment or example.Moreover, particular features, structures, materials, or characteristics described can be in office It can be combined in any suitable manner in one or more embodiment or examples.In addition, without conflicting with each other, the skill of this field Art personnel can tie the feature of different embodiments or examples described in this specification and different embodiments or examples It closes and combines.
In addition, term " first ", " second " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance Or implicitly indicate the quantity of indicated technical characteristic.Define " first " as a result, the feature of " second " can be expressed or Implicitly include at least one this feature.In the description of the present invention, the meaning of " plurality " is at least two, such as two, three It is a etc., unless otherwise specifically defined.
Any process described otherwise above or method description are construed as in flow chart or herein, and expression includes It is one or more for realizing custom logic function or process the step of executable instruction code module, segment or portion Point, and the range of the preferred embodiment of the present invention includes other realization, wherein can not press shown or discussed suitable Sequence, including according to related function by it is basic simultaneously in the way of or in the opposite order, Lai Zhihang function, this should be of the invention Embodiment person of ordinary skill in the field understood.
Expression or logic and/or step described otherwise above herein in flow charts, for example, being considered use In the order list for the executable instruction for realizing logic function, may be embodied in any computer-readable medium, for Instruction execution system, device or equipment (such as computer based system, including the system of processor or other can be held from instruction The instruction fetch of row system, device or equipment and the system executed instruction) it uses, or combine these instruction execution systems, device or set It is standby and use.For the purpose of this specification, " computer-readable medium ", which can be, any may include, stores, communicates, propagates or pass Defeated program is for instruction execution system, device or equipment or the dress used in conjunction with these instruction execution systems, device or equipment It sets.The more specific example (non-exhaustive list) of computer-readable medium include the following: there is the electricity of one or more wirings Interconnecting piece (electronic device), portable computer diskette box (magnetic device), random access memory (RAM), read-only memory (ROM), erasable edit read-only storage (EPROM or flash memory), fiber device and portable optic disk is read-only deposits Reservoir (CDROM).In addition, computer-readable medium can even is that the paper that can print described program on it or other are suitable Medium, because can then be edited, be interpreted or when necessary with it for example by carrying out optical scanner to paper or other media His suitable method is handled electronically to obtain described program, is then stored in computer storage.
It should be appreciated that each section of the invention can be realized with hardware, software, firmware or their combination.Above-mentioned In embodiment, software that multiple steps or method can be executed in memory and by suitable instruction execution system with storage Or firmware is realized.Such as, if realized with hardware in another embodiment, following skill well known in the art can be used Any one of art or their combination are realized: have for data-signal is realized the logic gates of logic function from Logic circuit is dissipated, the specific integrated circuit with suitable combinational logic gate circuit, programmable gate array (PGA), scene can compile Journey gate array (FPGA) etc..
Those skilled in the art are understood that realize all or part of step that above-described embodiment method carries It suddenly is that relevant hardware can be instructed to complete by program, the program can store in a kind of computer-readable storage medium In matter, which when being executed, includes the steps that one or a combination set of embodiment of the method.
It, can also be in addition, each functional unit in each embodiment of the present invention can integrate in a processing module It is that each unit physically exists alone, can also be integrated in two or more units in a module.Above-mentioned integrated mould Block both can take the form of hardware realization, can also be realized in the form of software function module.The integrated module is such as Fruit is realized and when sold or used as an independent product in the form of software function module, also can store in a computer In read/write memory medium.
Storage medium mentioned above can be read-only memory, disk or CD etc..Although having been shown and retouching above The embodiment of the present invention is stated, it is to be understood that above-described embodiment is exemplary, and should not be understood as to limit of the invention System, those skilled in the art can be changed above-described embodiment, modify, replace and become within the scope of the invention Type.

Claims (10)

1. a kind of energy recycling system of sewage characterized by comprising
Sewage draw-out device, the trade effluent for extracting high-temperature;
Heat-exchanger rig, the heat-exchanger rig include the first access and alternate path, and first access is for flowing through the industry Sewage, the alternate path are used to flow through the process water of low temperature, wherein the heat-exchanger rig be used for the trade effluent and The process water carries out heat exchange, to recycle the thermal energy of the trade effluent using the process water;
Controller, the controller are connected with the sewage draw-out device, are extracted with controlling the sewage of the sewage draw-out device Amount, adjusts the heat exchange efficiency of the heat-exchanger rig.
2. the energy recycling system of sewage according to claim 1, which is characterized in that the sewage draw-out device includes:
Filter, for filtering the impurity of the trade effluent, the upstream of the filter is equipped with sewage transfer puddle;
Sewage pump, for extracting sewage from sewage transfer puddle and being filled via the heat exchange is flow to after filter filtering It sets.
3. the energy recycling system of sewage according to claim 2, which is characterized in that the controller is used for according to At least one of the water level in sewage transfer puddle, flow velocity, temperature and pressure adjust the pump pressure of the sewage pump.
4. the energy recycling system of sewage according to claim 3, which is characterized in that sewage transfer puddle, which is equipped with, overflows Circulation road, the overflow ducts are connected with cesspool, reach the overflow ducts with the water level in sewage transfer puddle When, trade effluent is discharged into the cesspool automatically.
5. the energy recycling system of sewage according to claim 1, which is characterized in that further include:
Process water water pump, to adjust the flow for the process water for flowing through the alternate path, wherein the process water water pump It is controlled by the controller.
6. a kind of control method of the energy recycling system of sewage, which comprises the following steps:
Receive control signal;
According to the trade effluent of the control signal extraction high temperature, to carry out heat exchange to the trade effluent and process water, The thermal energy of the trade effluent is recycled using the process water.
7. the control method of the energy recycling system of sewage according to claim 6, which is characterized in that described according to Control the trade effluent of signal extraction high temperature, comprising:
Detect at least one of the water level, flow velocity, temperature and pressure of trade effluent;
At least one of water level, flow velocity, temperature and pressure according to the trade effluent adjust the extraction of the trade effluent Amount.
8. the control method of the energy recycling system of sewage according to claim 6, which is characterized in that further include:
The flow of process water is adjusted, to adjust the efficiency that the process water recycles the thermal energy of the trade effluent.
9. a kind of non-transitory readable storage medium storing program for executing, is stored thereon with computer program, which is characterized in that the computer program The control method of the energy recycling system of sewage a method according to any one of claims 6-8 is realized when being executed by processor.
10. a kind of apparatus for energy recovery of sewage, which is characterized in that including memory, processor and store on a memory simultaneously The energy recovery procedure for the sewage that can be run on a processor, the processor execute real when the energy recovery procedure of the sewage The control method of the energy recycling system of sewage described in any one of existing claim 6-8.
CN201910063650.3A 2019-01-23 2019-01-23 The energy recycling system and control method of sewage Pending CN109813166A (en)

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* Cited by examiner, † Cited by third party
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US4602672A (en) * 1981-03-05 1986-07-29 Thermal Engineering Of Arizona, Inc. Commercial laundry heat recovery system
WO2008067595A1 (en) * 2006-12-04 2008-06-12 Lomvac Technology Pty Ltd Method of heating and/or cooling
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