WO2018010197A1 - Odorous gas heat-exchange condensation system and method - Google Patents

Odorous gas heat-exchange condensation system and method Download PDF

Info

Publication number
WO2018010197A1
WO2018010197A1 PCT/CN2016/090669 CN2016090669W WO2018010197A1 WO 2018010197 A1 WO2018010197 A1 WO 2018010197A1 CN 2016090669 W CN2016090669 W CN 2016090669W WO 2018010197 A1 WO2018010197 A1 WO 2018010197A1
Authority
WO
WIPO (PCT)
Prior art keywords
odor
heat exchange
condenser
exhaust
exchange condenser
Prior art date
Application number
PCT/CN2016/090669
Other languages
French (fr)
Chinese (zh)
Inventor
汪深
匡文
方寅斗
刘运良
Original Assignee
湖南屎壳郎环境科技有限公司
汪深
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 湖南屎壳郎环境科技有限公司, 汪深 filed Critical 湖南屎壳郎环境科技有限公司
Publication of WO2018010197A1 publication Critical patent/WO2018010197A1/en

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28BSTEAM OR VAPOUR CONDENSERS
    • F28B1/00Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
    • F28B1/06Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using air or other gas as the cooling medium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/84Biological processes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B1/00Compression machines, plants or systems with non-reversible cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28BSTEAM OR VAPOUR CONDENSERS
    • F28B11/00Controlling arrangements with features specially adapted for condensers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Definitions

  • the invention belongs to the technical field of pollution treatment, and particularly relates to an organic waste fermentation odor heat exchange condensation system and method.
  • microorganisms In the process of organic waste fermentation, microorganisms oxidize some of the organic matter into simple inorganic substances through metabolic activities, providing the required energy for biological life activities, and converting another part of organic matter into nutrients required by the organism to form new ones. In the process of the cell body, the microorganisms continue to proliferate. In the process, a large amount of energy is released, except for a small part that provides energy for cytoplasmic synthesis, and the rest is released in the form of heat.
  • microbial oxidative decomposition The organic waste produces about 420kJ/kg of heat, which is discharged with the odor, so that the odor temperature can reach 60 ⁇ 70°C.
  • the evaporation rate of the material is accelerated, and a large amount of water is generated. Also discharged with the odor.
  • Mineral raw materials such as coal and diesel oil inevitably produce particulate matter such as smoke, carbon monoxide (CO), sulfur dioxide (SO 2 ) and nitrogen oxides (NO x ) in the combustion process.
  • particulate matter such as smoke, carbon monoxide (CO), sulfur dioxide (SO 2 ) and nitrogen oxides (NO x ) in the combustion process.
  • the combustion exhaust gas will also be taken away. A lot of heat, and this part of the heat is not used, causing waste of heat energy and increasing pollution to the environment.
  • the biological deodorization method is A odorless and harmless process method, which utilizes a microbial flora having a deodorizing function to convert odorous substances such as hydrogen sulfide and reduced sulfide in exhaust gas, has high removal rate, low running cost, and simple operation and management , It does not produce secondary pollution.
  • the deodorizing effect of biological deodorization depends on the activity of deodorizing microorganisms.
  • Deodorizing the intake air temperature is too high or too low, which will affect the growth and reproduction of microorganisms, thereby reducing the deodorizing effect and deodorizing.
  • the intake air temperature is higher than 40 ° C or lower than 15 ° C, the growth and reproduction of the deodorizing microorganism is inhibited; when the deodorizing air inlet temperature is higher than 60 ° C, the deodorizing microorganisms die in large amounts, and the deodorizing effect is lost.
  • the technical problem to be solved by the present invention is to solve the above problems in the prior art, and to provide an odor heat exchange condensation system and method, which satisfy the requirement that the biological deodorizing device controls the odor temperature at 10 ° C to 40 ° C, Avoiding excessive or too low temperature affecting the growth and reproduction of microorganisms and reducing the deodorizing effect, the system and method of the invention have large heat exchange surface area, high heat exchange efficiency, high intelligence of the detection and control device, and fresh air passing through the heat exchange condenser After heating, it can also be used as an organic waste for heat generation of aerobic fermentation and part of thermal energy of other thermal energy loads.
  • the invention not only saves energy but also protects the environment, and truly realizes the harmonious integration of pollution control and energy recycling.
  • the technical solution adopted by the invention is:
  • An odor heat exchange condensation system comprising a heat exchange condenser, a temperature sensor, a biological deodorizing device, a detection control device, an odor collecting pipe and an odor exhaust pipe, wherein the heat exchange condenser comprises a fixed connection
  • the upper end cover, the can body and the lower end cover have an odor inlet flange at the upper end of the upper end cover, and the odor collecting pipe is connected with the odor inlet flange;
  • the fresh air inlet method is arranged on the side wall of the tank body Lan, the upper part is provided with hot air exhaust flange; the hot air exhaust flange is connected to the thermal energy load through the hot air induced draft fan and the hot air duct;
  • the upper tube plate is installed on the upper part of the tank body, and the lower tube sheet is installed on the lower part, upper and lower A plurality of holes are evenly arranged on the tube plate, and are connected through the heat exchange tubes through the corresponding holes of the upper and lower tube sheets, and the two ends of the heat exchange tubes
  • a closed cavity is formed between the outside of the heat pipe and the outer wall of the can, and communicates with the outside through a fresh air intake flange and a hot air exhaust flange; a plurality of tie rods are uniformly fixed on the lower tube plate, and fresh air in the tank Inlet flange and hot air exhaust The space between the multiple baffles arranged uniformly, separated
  • the plate is fixed on the pull rod; the inner cavity of the heat exchange tube is connected to the upper and lower end covers; the bottom of the lower cover is provided with a U-shaped tube; the side wall of the lower end cover is provided with an odor exhaust flange, the odor exhaust flange and the odor
  • the exhaust pipe is fixedly connected, the odor exhaust pipe is connected to the inlet of the induced draft fan, the exhaust port of the induced draft fan is connected to the biological deodorizing device; and the bypass branch is connected between the odor collecting pipe and the inlet of the induced draft fan.
  • odor gas intake solenoid valve is installed at the end of the odor collecting pipe, temperature sensor is installed in the odor exhaust port or the odor exhaust pipe, and the output of the temperature sensor is connected to the signal input of the detecting control device And the control signal outputted by the detection control device is connected to the odor intake solenoid valve or the bypass branch solenoid valve.
  • the volume of the lower end cover is greater than or equal to the volume of the upper end cover.
  • the partition plate has a circular structure with a trimmed edge, and the diameter of the partition plate is equal to the inner diameter of the tank body.
  • the partition plate is scattered along the axial direction and uniformly distributed in the tank body, and the partition plate is fixed on the tie rod, so that the fresh air is oriented. It is a "Z" shape to increase the path of the air and increase the contact area between the air and the heat exchange tube.
  • the lower end cover water outlet is located at the lowest point of the lower end cover, and the lower end cover water outlet is connected to the water inlet of the U-shaped tube, and the highest liquid level of the U-shaped tube is lower than the lowest point of the odor exhaust flange.
  • the temperature control range in the odor exhaust port or the odor exhaust duct of the lower end of the heat exchange condenser set by the detecting control device is 10 ° C to 40 ° C, when the odor of the lower end of the heat exchange condenser
  • the detection control device outputs a control signal to open the odor intake solenoid valve above the upper end cover of the heat exchange condenser, and close the bypass branch electromagnetic a valve, wherein the odor is cooled by the heat exchange condenser and then enters the biological deodorizing device; and when the temperature sensor in the odor exhaust port or the odor exhaust pipe of the lower end of the heat exchange condenser detects that the odor temperature is less than 10 ° C,
  • the detection control device outputs a control signal to close the odor air intake electromagnetic valve above the upper end cover of the heat exchange condenser, opens the bypass branch electromagnetic valve, so that
  • An odor heat exchange condensation method comprising:
  • odor heat exchange condenser includes upper end cover, tank body and lower end cover which are connected in turn; odor gas inlet flange, odor gas collection pipe and odor on upper end of upper end cover
  • the intake flange is fixedly connected, and the odor gas intake solenoid valve is installed at the lower part of the odor collecting pipe, and the odor exhaust flange is provided at the bottom end of the lower end cover, and the odor exhaust flange is fixedly connected with the odor exhaust pipe, and the heat exchange is performed.
  • a temperature sensor is installed in the odor exhaust port or the odor exhaust pipe at the lower end of the condenser, and an air heat exchanger is installed in the tank body, and a hot air exhaust flange is arranged on the upper side of the tank side wall, and the tank side wall is provided a fresh air intake flange is provided at the lower portion;
  • the analog signal output from the temperature sensor of the lower end of the heat exchange condenser is connected to the input end of the detection control device, and the control signal outputted by the detection control device is connected to the odor air intake electromagnetic Valve or bypass branch solenoid valve;
  • the odor gas exhaust pipe connected to the lower end of the odor heat exchange condenser is connected with the inlet of the induced draft fan, and the exhaust fan exhaust port is connected to the biological deodorizing device, and the odor collecting pipe and the induced draft fan
  • a bypass branch and a bypass branch solenoid valve are also connected between the air inlets;
  • a fresh air intake flange at a lower portion of the side wall of the tank is a fresh cold air inlet, and a hot air exhaust method at the upper side of the tank side wall
  • the blue is connected to the thermal energy load through the hot air induced draft fan and the hot air pipe;
  • the U-shaped drain pipe is connected to the lower end of the heat exchange condenser;
  • the detection control device controls the odor gas intake solenoid valve on the intake pipe of the heat exchange condenser to be turned on, and the induced draft fan is started, and the odor gas is introduced into the heat exchange tube of the heat exchange condenser through the odor gas collection pipe, and the front end of the heat energy load is started.
  • the induced draft fan fresh air enters the outer circumference of the heat exchange tube of the heat exchange condenser through the fresh air inlet, and the hot odor in the heat exchange tube forms fresh convection with the fresh air outside the tube in the heat exchange condenser, and passes through the heat exchange tube
  • the wall undergoes sufficient heat exchange;
  • the odor is exchanged by the heat exchange condenser, cooled, discharged through the odor exhaust port, and then led to the organism by the induced draft fan.
  • the odor is absorbed and converted by the biological deodorizing device, and is discharged after reaching the standard; in addition, the fresh air heated by the heat exchange condenser is discharged from the hot air exhaust port and introduced into the thermal energy load to provide fresh heat load. Hot air
  • the detection control device When the temperature of the odor detected by the temperature sensor of the odor outlet of the heat exchange condenser is greater than 40 degrees, the detection control device outputs a control signal to open the odor intake solenoid valve on the intake pipe of the heat exchange condenser, Closing the bypass branch solenoid valve, so that the odor entering the biological deodorizing filter device is cooled in the heat exchange condenser; and when the temperature of the odor detected by the temperature sensor is less than 10 degrees, the detection control device outputs a control signal to turn off the heat exchange
  • the odor gas inlet solenoid valve of the condenser opens the bypass branch solenoid valve, so that the odor does not enter the heat exchanger condenser to cool down, so that the biological deodorizing device works in the temperature range of 10 ° C to 40 ° C, thereby ensuring the deodorizing effect.
  • the microorganisms in the biological deodorizing device are not to sleep and die.
  • the invention fully considers the characteristics of high odor of organic waste fermentation odor and high humidity, and creatively designs a heat exchange condenser, and several heat exchange tubes are uniformly arranged in the heat exchange condenser, and the heat exchange tube contains hot odor.
  • the gas is convected with the fresh air outside the pipe, and is fully exchanged by the heat exchange tube.
  • the heat exchange has a large specific surface area and high heat exchange efficiency, and at the same time, the fresh air is heated by the heat exchange condenser.
  • Hot air and hot air can be used as a heat source for organic waste to heat and supply organic waste, shorten the heating time of organic waste fermentation, and improve fermentation efficiency.
  • the invention is innovatively designed to provide a bypass branch on the heat exchanger condenser line.
  • the aerobic fermentation of organic waste, and the beginning of aerobic fermentation when the odor temperature is low, the low-temperature odor enters the biological deodorization device through the bypass branch to avoid the low-temperature odor passing through the heat exchange condenser again. Cooling; while in the high temperature stage of aerobic fermentation of organic waste, the odor of the discharged odor is high and the humidity is high.
  • the bypass branch is closed, and the odor is cooled by the heat exchange condenser to make the biological deodorizing filter tower
  • the temperature of the material is always kept within a limited range, which not only ensures the deodorizing effect, but also prevents the microorganisms in the biological deodorizing filter tower from sleeping and dying.
  • the invention not only saves energy but also protects the environment, and truly realizes the harmonious unification of pollution control and energy recycling.
  • Figure 1 is a schematic diagram of the principle of the present invention
  • FIG. 2 is a schematic structural view of a heat exchange condenser
  • Figure 3 is a schematic view showing the connection structure of the upper end cover and the can body
  • Figure 4 is a schematic view showing the connection structure of the lower end cover and the can body
  • Figure 5 is a partial enlarged view of Part I of Figure 4.
  • 201A odor gas intake solenoid valve
  • 202 heat exchange condenser
  • 203 hot air induced draft fan
  • 204 thermal load
  • 205 induced draft fan
  • 206 biological deodorizing device
  • 207 temperature sensor
  • 208 detection control device
  • 201B bypass branch solenoid valve
  • 101 upper end cap
  • 102 upper tube sheet
  • 103 heat exchange tube
  • 104 separator
  • 105 Te rod
  • 106 fresh air intake flange
  • 107 lower end cover
  • 108 odorous exhaust flange
  • 109 odor gas inlet flange
  • 110 hot air exhaust flange
  • an odor heat exchange condensation system of the present invention comprises a heat exchange condenser, a temperature sensor, a biological deodorizing device, a detection control device, an odor collecting pipe and an odor.
  • the exhaust pipe, the heat exchange condenser comprises an upper end cover, a tank body and a lower end cover which are sequentially connected, the upper end of the upper end cover has an odor air inlet flange, and the lower end of the odor collecting pipe is connected with the odor air inlet flange Fixed, the lower end of the lower end cover has an odor exhaust flange, the odor exhaust flange is connected with the odor exhaust pipe, the odor exhaust pipe is connected to the intake fan inlet, and the exhaust fan exhaust port is connected to the biological deodorization.
  • a bypass branch and a bypass branch solenoid valve are connected between the odor collecting pipe and the inlet of the induced draft fan; a fresh air intake flange is arranged at a lower portion of the side wall of the heat exchanger condenser
  • the upper part of the side wall of the heat exchange condenser is provided with a hot air exhaust flange, and the hot air exhaust flange is connected to the thermal energy load through the hot air induced draft fan and the hot air duct;
  • the air exchange is installed in the tank of the heat exchange condenser Heater;
  • odor gas is installed in the lower part of the odor collecting pipe
  • the gas solenoid valve is provided with a temperature sensor in the odor exhaust port or the odor exhaust pipe at the lower end of the heat exchange condenser, and the output of the temperature sensor is connected to the signal input end of the detection control device, and the control signal outputted by the detection control device is connected to A stinky intake solenoid valve or a bypass branch solenoid valve, wherein the air
  • the range is from 10 ° C to 40 ° C.
  • the odor air intake solenoid valve above the cover closes the bypass branch solenoid valve, so that the odor gas is cooled by the heat exchange condenser and then enters the biological deodorization device; and when the odor gas exhaust port or odor at the lower end of the heat exchange condenser
  • the detection control device outputs a control signal to close the odor air intake solenoid valve above the upper end cover of the heat exchange condenser, and opens the bypass branch solenoid valve to make the odor not Entering the heat exchange condenser to cool down;
  • the detection control device detects the odor exhaust temperature of the heat exchange condenser through the temperature sensor, and the output control signal of the detection control device controls the odor inlet solenoid valve or the bypass branch electromagnetic of the heat exchange condenser
  • the valve enables the biological deodorizing device to operate in a temperature range of 10 ° C to 40 ° C to ensure the deodorizing effect and avoid the dor
  • An odor heat exchange condensation method comprising:
  • odor heat exchange condenser includes upper end cover, tank body and lower end cover which are connected in turn; odor gas inlet flange, odor gas collection pipe and odor on upper end of upper end cover
  • the intake flange is fixedly connected, and the odor gas intake solenoid valve is installed at the lower part of the odor collecting pipe, and the odor exhaust flange is provided at the bottom end of the lower end cover, and the odor exhaust flange is fixedly connected with the odor exhaust pipe, and the heat exchange is performed.
  • a temperature sensor is installed in the odor exhaust port or the odor exhaust pipe at the lower end of the condenser, and an air heat exchanger is installed in the tank body, and a hot air exhaust flange is arranged on the upper side of the tank side wall, and the tank side wall is provided a fresh air intake flange is provided at the lower portion;
  • the analog signal output from the temperature sensor of the lower end of the heat exchange condenser is connected to the input end of the detection control device, and the control signal outputted by the detection control device is connected to the odor air intake electromagnetic Valve or bypass branch solenoid valve; odor exhaust pipe connected to the lower end of the odor heat exchange condenser The air inlet of the machine is connected, the exhaust port of the induced draft fan is connected with the biological deodorizing device, and the bypass branch and the bypass branch solenoid valve are connected between the odor collecting pipe and the inlet of the induced draft fan; the lower part of the side wall of the tank The fresh air intake flange is a fresh cold air inlet, and the hot air exhaust flange on the upper side of the tank side is connected to the thermal energy load through a hot air induced draft fan and a hot air duct; the water outlet connection U is connected to the lower end of the heat exchange condenser Type drain pipe;
  • the detection control device controls the odor gas intake solenoid valve on the intake pipe of the heat exchange condenser to be turned on, and the induced draft fan is started, and the odor gas is introduced into the heat exchange tube of the heat exchange condenser through the odor gas collection pipe, and the front end of the heat energy load is started.
  • the induced draft fan fresh air enters the outer circumference of the heat exchange tube of the heat exchange condenser through the fresh air inlet, and the hot odor in the heat exchange tube forms fresh convection with the fresh air outside the tube in the heat exchange condenser, and passes through the heat exchange tube
  • the wall undergoes sufficient heat exchange;
  • the odor gas is exchanged and exchanged by the heat exchange condenser, and then discharged through the odor exhaust port, and then introduced into the biological deodorizing device by the induced draft fan, and the odor is absorbed and converted by the biological deodorizing device, and discharged after reaching the standard;
  • the fresh air heated by the heat exchange condenser is discharged from the hot air exhaust port and introduced into the thermal energy load to provide fresh hot air for the thermal energy load;
  • the detection control device When the temperature of the odor detected by the temperature sensor of the odor outlet of the heat exchange condenser is greater than 40 degrees, the detection control device outputs a control signal to open the odor intake solenoid valve on the intake pipe of the heat exchange condenser, Closing the bypass branch solenoid valve, so that the odor entering the biological deodorizing filter device is cooled in the heat exchange condenser; and when the temperature of the odor detected by the temperature sensor is less than 10 degrees, the detection control device outputs a control signal to turn off the heat exchange
  • the odor gas inlet solenoid valve of the condenser opens the bypass branch solenoid valve, so that the odor does not enter the heat exchanger condenser to cool down, so that the biological deodorizing device works in the temperature range of 10 ° C to 40 ° C, thereby ensuring the deodorizing effect. And let the creatures The microorganisms in the stinky device do not sleep and die.
  • the schematic diagram of the heat exchange condenser according to the present invention is shown in FIG. 2.
  • the heat exchange condenser is sequentially composed of an upper end cover 101, an upper tube sheet 102, a can body 111, a lower tube sheet 112, a lower end cover 107 and U from top to bottom.
  • the tube 113 is formed, and a plurality of air holes are evenly arranged on the upper tube plate 102 and the lower tube plate 112.
  • the upper tube plate 102 and the lower tube plate 112 are connected by a heat exchange tube 103 corresponding to the air holes, and a plurality of tie rods 105 are fixed on the lower tube plate 112.
  • a plurality of trimmed partitions 104 are arranged evenly between the air inlet and outlet, and the partition 104 is fixed on the pull rod 105.
  • the diameter of the partition 104 is smaller than the inner diameter of the tank 111, and the upper end cover 101 is provided with The odor air intake flange 109, the upper end of the lower end cover 107 is provided with an odor exhaust flange 108, the lower part of the side wall of the tank body 111 is provided with a cold air intake flange 106, and the upper part of the side wall of the tank body 111 is provided with a hot air exhaust line
  • the gas flange 110, the water inlet of the U-shaped tube 113 is fixed at the bottom of the lower end cover 107, and the highest liquid level of the U-shaped tube 113 is lower than the lowest point of the odor exhaust flange 108.
  • An odor heat exchange condensing device and method mainly comprises a heat exchange condenser 202, electromagnetic valves 201A and 201B, induced draft fans 203 and 205, and thermal energy load.
  • the odor inlet flange 109 of the heat exchange condenser 202 is connected to the odor collecting pipe, and the odor exhausting flange 108
  • the air inlet of the induced draft fan 205 is connected via an exhaust duct, and a temperature sensor 207 is installed at the odor exhaust port, and the exhaust port of the induced draft fan 205 is connected to the air inlet of the biological deodorizing device 206 via a pipeline, in the heat exchange condenser
  • the solenoid valve 201A is provided with a solenoid valve 201A, and a bypass branch is provided.
  • the bypass branch of the odor heat exchange condenser 202 is provided with a solenoid valve 201B, and the hot air exhaust flange 110 of the heat exchange condenser 202 is
  • the pipe is connected to the intake port of the induced draft fan 203, and the exhaust port of the induced draft fan 203 is connected to the intake port of the thermal energy load 204 via a pipe.
  • the detection control device control 208 opens the electromagnetic valve 201A on the intake pipe of the odor heat exchange condenser, activates the induced draft fan 205, and the odor is introduced into the heat exchange tube of the heat exchange condenser 202 via the odor inlet flange 109.
  • the induced draft fan 203 of the front stage of the thermal energy load 204 is started, and the fresh air enters the heat exchange tube 103 of the heat exchange condenser 202 via the fresh air intake flange 106, and the heat exchange tube 103 contains the hot odor and the heat exchange tube 103.
  • the fresh air outside the tube forms convection in the heat exchange condenser 202, and is fully heat exchanged through the tube wall of the heat exchange tube 202;
  • the odor is exchanged and exchanged by the heat exchange condenser 202, and then discharged through the odor exhaust flange 108, and then introduced into the biological deodorizing device 206 through the air inlet of the biological deodorizing device 206, and the odor is passed through the living body.
  • the deodorizing device 206 absorbs, converts, and discharges after reaching the standard; the air heated by the heat exchange condenser 202 is discharged from the hot air exhaust flange 110, introduced into the thermal energy load 204 via the induced draft fan 203, and provides fresh heat to the thermal energy load 204. air;
  • the detection control device 208 When the detection control device 208 detects that the temperature sensor 207 installed in the odor exhaust port of the heat exchange condenser 202 detects that the odor temperature is greater than 40 degrees, the detection control device 208 opens the intake of the odor heat exchange condenser 202.
  • the solenoid valve 201A on the pipe closes the bypass branch solenoid valve 201B, so that the odor entering the biological deodorizing device 206 is cooled by the odor heat exchange condenser 202; and when the detecting control device 208 detects the installation in the heat exchange condenser 202 When the temperature sensor 207 of the odor exhaust port detects that the temperature of the deodorizing filler in the biological deodorizing device 206 is less than 10 degrees, the control system 208 turns off the solenoid valve 201A on the intake pipe of the heat exchange condenser 202, and opens the bypass branch.
  • the road electromagnetic valve 201B prevents the odor from entering the heat exchange condenser 202 to cool down, so that the biological deodorizing device 206 operates in the temperature range of 10 ° C to 40 ° C, thereby ensuring the deodorizing effect and preventing the microorganisms in the biological deodorizing device 206 from being As for dormancy and death.

Abstract

An odorous gas heat-exchange condensation system and method. An odorous gas collecting pipe is connectively fixed to an odorous gas intake flange (109) of an upper end cover (101) of a heat-exchange condenser (202). An odorous gas exhaust flange (108) of a lower end cover (107) of the heat-exchange condenser (202) is connectively fixed to an odorous gas exhaust pipe. The odorous gas exhaust pipe is connected to a biological deodorization apparatus (206) via an induced draft fan (205). A bypass and a bypass solenoid valve (210B) are connected between the odorous gas collecting pipe and an air inlet of the induced draft fan (205). A fresh air intake flange (106) and a hot air exhaust flange (110) are provided at the upper and lower parts of the sidewall of a tank body (111) of the heat-exchange condenser (202). The hot air exhaust flange (110) is connected to a heat load (204). A detection and control device is connected to a temperature sensor mounted at an odorous gas exhaust outlet at the lower end of the heat-exchange condenser (202) and is connected to an odorous gas intake solenoid valve (210A) or to the bypass solenoid valve (210B) so as to control the biological deodorization apparatus in the optimal temperature of 10-40 °C.

Description

一种臭气换热冷凝系统及方法Odor heat exchange condensation system and method 技术领域Technical field
本发明属于污染治理技术领域,具体涉及一种有机废弃物发酵臭气换热冷凝系统及方法。The invention belongs to the technical field of pollution treatment, and particularly relates to an organic waste fermentation odor heat exchange condensation system and method.
背景技术Background technique
在工农业生产、污水处理、垃圾处理和堆肥等过程中,会产生大量的臭气和有机废气,不但对周围环境造成污染,同时对人体健康和生态环境造成严重危害,臭气和有机废气的治理越来越受到人们的关注。In the process of industrial and agricultural production, sewage treatment, garbage treatment and composting, a large amount of odor and organic waste gas will be generated, which will not only pollute the surrounding environment, but also cause serious harm to human health and ecological environment, odor and organic waste gas. Governance is getting more and more attention.
在有机废弃物发酵过程中,微生物通过代谢活动,把其中一部分有机物氧化成简单的无机物,为生物生命活动提供所需的能量,另一部分有机物转化为生物体所需的营养物质,形成新的细胞体,使微生物不断增殖,在此过程中,放出大量能量,除小部分为细胞质合成提供能量外,其余均以热量的形式放出,据文献介绍,在有机废弃物高温发酵阶段,微生物氧化分解有机废弃物平产生的热量约420kJ/kg,这些热能随臭气排出,使臭气温度最高可达60~70℃,同时,由于物料堆体温度升高,导致物料水分蒸发速度加快,大量水分也随臭气排出。In the process of organic waste fermentation, microorganisms oxidize some of the organic matter into simple inorganic substances through metabolic activities, providing the required energy for biological life activities, and converting another part of organic matter into nutrients required by the organism to form new ones. In the process of the cell body, the microorganisms continue to proliferate. In the process, a large amount of energy is released, except for a small part that provides energy for cytoplasmic synthesis, and the rest is released in the form of heat. According to the literature, in the high-temperature fermentation stage of organic waste, microbial oxidative decomposition The organic waste produces about 420kJ/kg of heat, which is discharged with the odor, so that the odor temperature can reach 60~70°C. At the same time, due to the increase of the temperature of the material pile, the evaporation rate of the material is accelerated, and a large amount of water is generated. Also discharged with the odor.
矿质原料如煤炭、柴油等在燃烧过程中不可避免地产生烟尘等颗粒物、一氧化碳(CO)、二氧化硫(SO2)和氮氧化物(NOx)等有毒有害气体,同时,燃烧尾气也会带走大量热量,而这部分热量未经利用,造成热能的浪费,加剧对环境的污染。Mineral raw materials such as coal and diesel oil inevitably produce particulate matter such as smoke, carbon monoxide (CO), sulfur dioxide (SO 2 ) and nitrogen oxides (NO x ) in the combustion process. At the same time, the combustion exhaust gas will also be taken away. A lot of heat, and this part of the heat is not used, causing waste of heat energy and increasing pollution to the environment.
治理臭气和有机废气的技术有很多,如吸收吸附、焚烧法、化学转化法、冷凝法及生物法等,但在这些方法中,最为经济有效的是生物除臭法,生物除臭法是一种无臭化、无害化的工艺方法,即利用具有除臭功能的微生物菌群转化废气中的硫化氢、还原硫化物等臭气物质,具有去除率高,运转费用低,操作管理简单, 不产生二次污染等优点,但是,生物除臭法除臭效果依赖除臭微生物的活性,除臭进气温度过高或过低都会影响微生物的生长繁殖,进而降低除臭效果,当除臭进气温度高于40℃或低于15℃时,除臭微生物生长繁殖受到抑制;当除臭进气温度高于60℃时,除臭微生物大量死亡,丧失除臭效果。There are many technologies for controlling odor and organic waste gas, such as absorption and adsorption, incineration, chemical conversion, condensation, and biological methods. However, among these methods, the most economical and effective one is biological deodorization. The biological deodorization method is A odorless and harmless process method, which utilizes a microbial flora having a deodorizing function to convert odorous substances such as hydrogen sulfide and reduced sulfide in exhaust gas, has high removal rate, low running cost, and simple operation and management , It does not produce secondary pollution. However, the deodorizing effect of biological deodorization depends on the activity of deodorizing microorganisms. Deodorizing the intake air temperature is too high or too low, which will affect the growth and reproduction of microorganisms, thereby reducing the deodorizing effect and deodorizing. When the intake air temperature is higher than 40 ° C or lower than 15 ° C, the growth and reproduction of the deodorizing microorganism is inhibited; when the deodorizing air inlet temperature is higher than 60 ° C, the deodorizing microorganisms die in large amounts, and the deodorizing effect is lost.
发明内容Summary of the invention
本发明所要解决的技术问题是:解决上述现有技术存在的问题,而提供一种臭气换热冷凝系统及方法,满足生物除臭装置对于臭气温度控制在10℃~40℃的要求,避免温度过高或过低影响微生物的生长繁殖,降低除臭效果,本发明的系统及方法换热比表面积大,换热效率高,检测控制装置智能化程度高,新鲜空气经换热冷凝器加热后还可作为有机废弃物进行好氧发酵的热源和其他热能负载的部分热能,本发明既节能,又环保,真正实现污染治理与能源循环利用和谐统一。本发明采用的技术方案是:The technical problem to be solved by the present invention is to solve the above problems in the prior art, and to provide an odor heat exchange condensation system and method, which satisfy the requirement that the biological deodorizing device controls the odor temperature at 10 ° C to 40 ° C, Avoiding excessive or too low temperature affecting the growth and reproduction of microorganisms and reducing the deodorizing effect, the system and method of the invention have large heat exchange surface area, high heat exchange efficiency, high intelligence of the detection and control device, and fresh air passing through the heat exchange condenser After heating, it can also be used as an organic waste for heat generation of aerobic fermentation and part of thermal energy of other thermal energy loads. The invention not only saves energy but also protects the environment, and truly realizes the harmonious integration of pollution control and energy recycling. The technical solution adopted by the invention is:
一种臭气换热冷凝系统,包括换热冷凝器、温度传感器、生物除臭装置、检测控制装置、臭气收集管道和臭气排气管道,所述的换热冷凝器包括依次连接固定的上端盖、罐体、下端盖,上端盖的上端具有臭气进气法兰,臭气收集管道与臭气进气法兰连接固定;在罐体侧壁上,下部设有新鲜空气进气法兰,上部设有热空气排气法兰;热空气排气法兰通过热空气引风机及热空气管道连接热能负载;在罐体上部安装有上管板,下部安装下管板,上、下管板上均匀布置有若干孔,穿过上、下管板的对应孔之间用换热管连接,换热管两端分别固定在上、下管板上,使上、下管板、换热管外侧和罐体外壁之间形成一个密闭腔体,并通过新鲜空气进气法兰和热空气排气法兰与外界连通;在下管板上均匀固定多根拉杆,在罐体内的新鲜空气进气法兰和热空气排气法兰之间的空间内均匀布置有多块隔板,隔 板固定在拉杆上;换热管内腔连通上、下端盖;下盖板底部设置有U形管;下端盖的侧壁上设有臭气排气法兰,臭气排气法兰与臭气排气管道连接固定,臭气排气管道连接引风机进气口,引风机排气口连接生物除臭装置;在臭气收集管道与引风机进气口之间还连接有旁通支路及旁通支路电磁阀;臭气收集管道末端安装有臭气进气电磁阀,在臭气排气口或臭气排气管道内安装有温度传感器,温度传感器的输出连接检测控制装置的信号输入端,而检测控制装置输出的控制信号连接臭气进气电磁阀或旁通支路电磁阀。An odor heat exchange condensation system, comprising a heat exchange condenser, a temperature sensor, a biological deodorizing device, a detection control device, an odor collecting pipe and an odor exhaust pipe, wherein the heat exchange condenser comprises a fixed connection The upper end cover, the can body and the lower end cover have an odor inlet flange at the upper end of the upper end cover, and the odor collecting pipe is connected with the odor inlet flange; the fresh air inlet method is arranged on the side wall of the tank body Lan, the upper part is provided with hot air exhaust flange; the hot air exhaust flange is connected to the thermal energy load through the hot air induced draft fan and the hot air duct; the upper tube plate is installed on the upper part of the tank body, and the lower tube sheet is installed on the lower part, upper and lower A plurality of holes are evenly arranged on the tube plate, and are connected through the heat exchange tubes through the corresponding holes of the upper and lower tube sheets, and the two ends of the heat exchange tubes are respectively fixed on the upper and lower tube sheets, so that the upper and lower tube sheets are replaced. A closed cavity is formed between the outside of the heat pipe and the outer wall of the can, and communicates with the outside through a fresh air intake flange and a hot air exhaust flange; a plurality of tie rods are uniformly fixed on the lower tube plate, and fresh air in the tank Inlet flange and hot air exhaust The space between the multiple baffles arranged uniformly, separated The plate is fixed on the pull rod; the inner cavity of the heat exchange tube is connected to the upper and lower end covers; the bottom of the lower cover is provided with a U-shaped tube; the side wall of the lower end cover is provided with an odor exhaust flange, the odor exhaust flange and the odor The exhaust pipe is fixedly connected, the odor exhaust pipe is connected to the inlet of the induced draft fan, the exhaust port of the induced draft fan is connected to the biological deodorizing device; and the bypass branch is connected between the odor collecting pipe and the inlet of the induced draft fan. Bypass branch solenoid valve; odor gas intake solenoid valve is installed at the end of the odor collecting pipe, temperature sensor is installed in the odor exhaust port or the odor exhaust pipe, and the output of the temperature sensor is connected to the signal input of the detecting control device And the control signal outputted by the detection control device is connected to the odor intake solenoid valve or the bypass branch solenoid valve.
上述技术方案中,下端盖的的容积大于或等于上端盖的容积。In the above technical solution, the volume of the lower end cover is greater than or equal to the volume of the upper end cover.
上述技术方案中,隔板为切边的圆形结构,隔板的直径等于罐体的内径,隔板沿轴线方向错落、均匀地分布于罐体内,隔板固定在拉杆上,使得新鲜空气走向为“Z”字型,以增加空气的路径,增大空气与换热管的接触面积。In the above technical solution, the partition plate has a circular structure with a trimmed edge, and the diameter of the partition plate is equal to the inner diameter of the tank body. The partition plate is scattered along the axial direction and uniformly distributed in the tank body, and the partition plate is fixed on the tie rod, so that the fresh air is oriented. It is a "Z" shape to increase the path of the air and increase the contact area between the air and the heat exchange tube.
上述技术方案中,所述的下端盖出水口位于下端盖的最低处,下端盖出水口连接U型管的进水口,U型管的最高液位低于臭气排气法兰的最低点。In the above technical solution, the lower end cover water outlet is located at the lowest point of the lower end cover, and the lower end cover water outlet is connected to the water inlet of the U-shaped tube, and the highest liquid level of the U-shaped tube is lower than the lowest point of the odor exhaust flange.
上述技术方案中,所述的检测控制装置设定的换热冷凝器下端臭气排气口或臭气排气管道内的温度控制范围为10℃~40℃,当换热冷凝器下端臭气排气口或臭气排气管内的温度传感器检测到臭气温度大于40℃时,检测控制装置输出控制信号打开换热冷凝器上端盖上方的臭气进气电磁阀,关闭旁通支路电磁阀,使臭气经换热冷凝器冷却后再进入生物除臭装置;而当换热冷凝器下端臭气排气口或臭气排气管内的温度传感器检测到臭气温度小于10℃时,检测控制装置输出控制信号关闭换热冷凝器上端盖上方的臭气进气电磁阀,打开旁通支路电磁阀,使臭气不进入换热冷凝器降温;检测控制装置通过温度传感器检测换热冷凝器的臭气排气温度,检测控制装置输出控制信号控制换热冷凝器的臭气进气电磁阀或旁通支 路电磁阀,使生物除臭装置在10℃~40℃温度区间工作,既保证除臭效果,又避免生物除臭装置中微生物的休眠和死亡。In the above technical solution, the temperature control range in the odor exhaust port or the odor exhaust duct of the lower end of the heat exchange condenser set by the detecting control device is 10 ° C to 40 ° C, when the odor of the lower end of the heat exchange condenser When the temperature sensor in the exhaust port or the odor exhaust pipe detects that the odor temperature is greater than 40 ° C, the detection control device outputs a control signal to open the odor intake solenoid valve above the upper end cover of the heat exchange condenser, and close the bypass branch electromagnetic a valve, wherein the odor is cooled by the heat exchange condenser and then enters the biological deodorizing device; and when the temperature sensor in the odor exhaust port or the odor exhaust pipe of the lower end of the heat exchange condenser detects that the odor temperature is less than 10 ° C, The detection control device outputs a control signal to close the odor air intake electromagnetic valve above the upper end cover of the heat exchange condenser, opens the bypass branch electromagnetic valve, so that the odor does not enter the heat exchange condenser to cool down; the detection control device detects the heat exchange through the temperature sensor The odor exhaust temperature of the condenser, the output control signal of the detection control device controls the odor inlet solenoid valve or the bypass branch of the heat exchange condenser The road electromagnetic valve enables the biological deodorizing device to work in a temperature range of 10 ° C to 40 ° C to ensure the deodorizing effect and avoid the dormancy and death of microorganisms in the biological deodorizing device.
一种臭气换热冷凝方法,包括:An odor heat exchange condensation method comprising:
(1)设计制造臭气换热冷凝器:臭气换热冷凝器包括依次连接固定的上端盖、罐体、下端盖;上端盖上端具有臭气进气法兰,臭气收集管道与臭气进气法兰连接固定,臭气收集管道下部安装有臭气进气电磁阀,下端盖底端具有臭气排气法兰,臭气排气法兰与臭气排气管道连接固定,换热冷凝器下端臭气排气口或臭气排气管道内安装有温度传感器,所述罐体内安装有空气换热器,在罐体侧壁上部设有热空气排气法兰,罐体侧壁下部设有新鲜空气进气法兰;(1) Design and manufacture of odor heat exchange condenser: odor heat exchange condenser includes upper end cover, tank body and lower end cover which are connected in turn; odor gas inlet flange, odor gas collection pipe and odor on upper end of upper end cover The intake flange is fixedly connected, and the odor gas intake solenoid valve is installed at the lower part of the odor collecting pipe, and the odor exhaust flange is provided at the bottom end of the lower end cover, and the odor exhaust flange is fixedly connected with the odor exhaust pipe, and the heat exchange is performed. A temperature sensor is installed in the odor exhaust port or the odor exhaust pipe at the lower end of the condenser, and an air heat exchanger is installed in the tank body, and a hot air exhaust flange is arranged on the upper side of the tank side wall, and the tank side wall is provided a fresh air intake flange is provided at the lower portion;
(2)连接臭气换热冷凝系统:换热冷凝器下端臭气排气口的温度传感器输出的模拟信号连接至检测控制装置输入端,检测控制装置输出的控制信号连接至臭气进气电磁阀或旁通支路电磁阀;臭气换热冷凝器下端连接的臭气排气管道与引风机进气口连接,引风机排气口连接生物除臭装置,在臭气收集管道与引风机进气口之间还连接有旁通支路及旁通支路电磁阀;罐体侧壁下部的新鲜空气进气法兰为新鲜冷空气入口,而罐体侧壁上部的热空气排气法兰通过热空气引风机及热空气管道连接热能负载;在换热冷凝器下端盖出水口连接U型排水管;(2) Connecting the odor heat exchange condensation system: the analog signal output from the temperature sensor of the lower end of the heat exchange condenser is connected to the input end of the detection control device, and the control signal outputted by the detection control device is connected to the odor air intake electromagnetic Valve or bypass branch solenoid valve; the odor gas exhaust pipe connected to the lower end of the odor heat exchange condenser is connected with the inlet of the induced draft fan, and the exhaust fan exhaust port is connected to the biological deodorizing device, and the odor collecting pipe and the induced draft fan A bypass branch and a bypass branch solenoid valve are also connected between the air inlets; a fresh air intake flange at a lower portion of the side wall of the tank is a fresh cold air inlet, and a hot air exhaust method at the upper side of the tank side wall The blue is connected to the thermal energy load through the hot air induced draft fan and the hot air pipe; the U-shaped drain pipe is connected to the lower end of the heat exchange condenser;
(3)检测控制装置控制开启换热冷凝器的进气管道上的臭气进气电磁阀,启动引风机,臭气经臭气收集管道引入换热冷凝器的换热管内,启动热能负载前端的引风机,新鲜空气经新鲜空气进气口进入换热冷凝器的换热管外周,换热管内含热臭气与管外的新鲜空气在换热冷凝器内形成对流,通过换热管管壁进行充分的热交换;(3) The detection control device controls the odor gas intake solenoid valve on the intake pipe of the heat exchange condenser to be turned on, and the induced draft fan is started, and the odor gas is introduced into the heat exchange tube of the heat exchange condenser through the odor gas collection pipe, and the front end of the heat energy load is started. The induced draft fan, fresh air enters the outer circumference of the heat exchange tube of the heat exchange condenser through the fresh air inlet, and the hot odor in the heat exchange tube forms fresh convection with the fresh air outside the tube in the heat exchange condenser, and passes through the heat exchange tube The wall undergoes sufficient heat exchange;
(4)臭气经换热冷凝器换热、冷却后经臭气排气口排出,再经引风机引至生物 除臭装置内,臭气经生物除臭装置吸收、转化,达标后排放;另外,将经换热冷凝器加热的新鲜空气从热空气排气口排出,引入热能负载中,为热能负载提供新鲜的热空气;(4) The odor is exchanged by the heat exchange condenser, cooled, discharged through the odor exhaust port, and then led to the organism by the induced draft fan. In the deodorizing device, the odor is absorbed and converted by the biological deodorizing device, and is discharged after reaching the standard; in addition, the fresh air heated by the heat exchange condenser is discharged from the hot air exhaust port and introduced into the thermal energy load to provide fresh heat load. Hot air
(5)臭气经换热冷凝器降温后产生的冷凝水汇集在换热冷凝器的下端盖中,当下端盖中的冷凝水液位达到一定值时,由于压差作用,冷凝水自动从U型管排水口排至沟渠中;(5) The condensed water generated by the odor gas cooled by the heat exchange condenser is collected in the lower end cover of the heat exchange condenser. When the condensed water level in the lower end cap reaches a certain value, the condensed water is automatically removed due to the pressure difference. The U-shaped pipe drain is discharged into the ditch;
(6)当换热冷凝器臭气排气口的温度传感器所检测的臭气温度大于40度时,检测控制装置输出控制信号打开换热冷凝器进气管道上的臭气进气电磁阀,关闭旁通支路电磁阀,使进入生物除臭滤装置的臭气在换热冷凝器内冷却;而当温度传感器所检测的臭气温度小于10度时,检测控制装置输出控制信号关闭换热冷凝器的臭气进气电磁阀,打开旁通支路电磁阀,使臭气不进入换热冷凝器内降温,使生物除臭装置在10℃至40℃温度区间工作,既保证除臭效果,又使生物除臭装置中的微生物不至于休眠和死亡。(6) When the temperature of the odor detected by the temperature sensor of the odor outlet of the heat exchange condenser is greater than 40 degrees, the detection control device outputs a control signal to open the odor intake solenoid valve on the intake pipe of the heat exchange condenser, Closing the bypass branch solenoid valve, so that the odor entering the biological deodorizing filter device is cooled in the heat exchange condenser; and when the temperature of the odor detected by the temperature sensor is less than 10 degrees, the detection control device outputs a control signal to turn off the heat exchange The odor gas inlet solenoid valve of the condenser opens the bypass branch solenoid valve, so that the odor does not enter the heat exchanger condenser to cool down, so that the biological deodorizing device works in the temperature range of 10 ° C to 40 ° C, thereby ensuring the deodorizing effect. Moreover, the microorganisms in the biological deodorizing device are not to sleep and die.
有益效果:Beneficial effects:
本发明充分考虑有机废弃物发酵臭气热量高、湿度大的特点,创造性地设计一种换热冷凝器,换热冷凝器内均匀竖直排列中若干个换热管,换热管内含热臭气与管外的新鲜空气对流,通过换热管进行充分地热交换,该方式与传统换热方式相比,换热比表面积大,换热效率高,同时,新鲜空气经换热冷凝器加热成热空气,热空气可以作为有机废弃物的热源,对有机废弃物进行加热、供氧,缩短有机废弃物发酵升温时间,提高发酵效率。The invention fully considers the characteristics of high odor of organic waste fermentation odor and high humidity, and creatively designs a heat exchange condenser, and several heat exchange tubes are uniformly arranged in the heat exchange condenser, and the heat exchange tube contains hot odor. The gas is convected with the fresh air outside the pipe, and is fully exchanged by the heat exchange tube. Compared with the conventional heat exchange mode, the heat exchange has a large specific surface area and high heat exchange efficiency, and at the same time, the fresh air is heated by the heat exchange condenser. Hot air and hot air can be used as a heat source for organic waste to heat and supply organic waste, shorten the heating time of organic waste fermentation, and improve fermentation efficiency.
由于有机废弃物发酵臭气湿度大,在经换热冷凝器降温的同时,也产生了大量大量冷凝水,这些冷凝水经换热管自然汇集到换热冷凝器的下端盖内,当冷凝水 液位达到一定高度时,由于压差的作用,冷凝水随U型管自然外排至沟渠中,这种方式操作简单易行,同时利用冷凝水密封下端盖冷凝水排水口,防止冷凝后的臭气经下端盖冷凝水排水口排向大气造成二次污染。Due to the high humidity of the organic waste fermentation odor, a large amount of condensed water is also generated while being cooled by the heat exchange condenser, and the condensed water is naturally collected into the lower end cover of the heat exchange condenser through the heat exchange tube, when the condensed water When the liquid level reaches a certain height, due to the pressure difference, the condensed water is naturally discharged into the ditch along with the U-shaped pipe. This method is simple and easy to operate, and the condensed water drain port of the lower end cover is sealed by the condensed water to prevent condensation. The odor is discharged to the atmosphere through the lower end cover condensate drain port to cause secondary pollution.
当在冬季进行有机废弃物的好氧发酵,以及好氧发酵伊始,排出的臭气温度低时,无需换热冷凝,本发明创新设计,在换热冷凝器管路上设置旁通支路,当在冬季进行有机废弃物的好氧发酵,以及好氧发酵伊始,排出的臭气温度低时,低温臭气经过旁通支路进入生物除臭装置,以避免低温臭气经过换热冷凝器再次降温;而当在有机废弃物的好氧发酵的高温阶段,排出的臭气温度高、湿度大,此时关闭旁通支路,臭气通过换热冷凝器降温,使生物除臭滤塔内物料温度始终保持在限定的范围内,既保证除臭效果,又使生物除臭滤塔中的微生物不至于休眠和死亡。When the aerobic fermentation of organic waste is carried out in winter, and the temperature of the discharged odor is low at the beginning of aerobic fermentation, heat exchange condensation is not required, and the invention is innovatively designed to provide a bypass branch on the heat exchanger condenser line. In the winter, the aerobic fermentation of organic waste, and the beginning of aerobic fermentation, when the odor temperature is low, the low-temperature odor enters the biological deodorization device through the bypass branch to avoid the low-temperature odor passing through the heat exchange condenser again. Cooling; while in the high temperature stage of aerobic fermentation of organic waste, the odor of the discharged odor is high and the humidity is high. At this time, the bypass branch is closed, and the odor is cooled by the heat exchange condenser to make the biological deodorizing filter tower The temperature of the material is always kept within a limited range, which not only ensures the deodorizing effect, but also prevents the microorganisms in the biological deodorizing filter tower from sleeping and dying.
本发明既节能,又环保,真正实现污染治理与能源循环利用的和谐统一。The invention not only saves energy but also protects the environment, and truly realizes the harmonious unification of pollution control and energy recycling.
附图说明:BRIEF DESCRIPTION OF THE DRAWINGS:
图1为本发明原理示意图;Figure 1 is a schematic diagram of the principle of the present invention;
图2为换热冷凝器结构示意图;2 is a schematic structural view of a heat exchange condenser;
图3上端盖与罐体连接结构示意图;Figure 3 is a schematic view showing the connection structure of the upper end cover and the can body;
图4下端盖与罐体连接结构示意图;Figure 4 is a schematic view showing the connection structure of the lower end cover and the can body;
图5为图4中I局部放大图。Figure 5 is a partial enlarged view of Part I of Figure 4.
附图标记说明:Description of the reference signs:
201A—臭气进气电磁阀,202—换热冷凝器,203—热空气引风机,204—热能负载,205—引风机,206—生物除臭装置,207—温度传感器,208—检测控制装置,201B—旁通支路电磁阀,101—上端盖,102—上管板,103—换热管,104—隔板, 105—拉杆,106—新鲜空气进气法兰,107—下端盖,108—臭气排气法兰,109—臭气进气法兰,110—热空气排气法兰,111—罐体,112—下管板,113—U型管。201A—odor gas intake solenoid valve, 202—heat exchange condenser, 203—hot air induced draft fan, 204—thermal load, 205—induced draft fan, 206—biological deodorizing device, 207—temperature sensor, 208—detection control device , 201B—bypass branch solenoid valve, 101—upper end cap, 102—upper tube sheet, 103—heat exchange tube, 104—separator, 105—Tie rod, 106—fresh air intake flange, 107—lower end cover, 108—odorous exhaust flange, 109—odor gas inlet flange, 110—hot air exhaust flange, 111—tank, 112 - lower tube sheet, 113 - U tube.
具体实施方式:detailed description:
参见图1、图2、图3和图4,本发明的一种臭气换热冷凝系统,包括换热冷凝器、温度传感器、生物除臭装置、检测控制装置、臭气收集管道和臭气排气管道,所述的换热冷凝器包括依次连接固定的上端盖、罐体、下端盖,上端盖的上端具有臭气进气法兰,臭气收集管道下端与臭气进气法兰连接固定,下端盖的下端具有臭气排气法兰,臭气排气法兰与臭气排气管道连接固定,臭气排气管连接引风机进气口,引风机排气口连接生物除臭装置;在臭气收集管道与引风机进气口之间还连接有旁通支路及旁通支路电磁阀;所述换热冷凝器的罐体侧壁下部设有新鲜空气进气法兰,换热冷凝器的罐体侧壁上部设有热空气排气法兰,热空气排气法兰通过热空气引风机及热空气管道连接热能负载;在换热冷凝器的罐体内安装空气换热器;臭气收集管道下部安装有臭气进气电磁阀,在换热冷凝器下端臭气排气口或臭气排气管道内安装有温度传感器,温度传感器的输出连接检测控制装置的信号输入端,而检测控制装置输出的控制信号连接至臭进气电磁阀或旁通支路电磁阀,所述换热冷凝器罐体内安装的空气换热器为列管式热交换器,具体结构为:在罐体内上部安装上管板,在罐体内下部安装下管板,上管板上和下管板上均匀布置很多气孔,上管板和下管板的对应气孔间用换热管连接,换热管内腔与臭气连通,换热管外侧空间与新鲜空气连通,在下管板上固定多根拉杆,在罐体内的新鲜空气进气和热空气排气之间的空间内均匀布置有多块切边的隔板,隔板的直径等于罐体的内径,隔板沿轴线方向错落地固定在拉杆上,所述的下端盖出 水口连接U型管的进水口,U型管的排水口位置低于下端盖,所述的检测控制装置设定的换热冷凝器下端臭气排气口或臭气排气管道内的温度控制范围为10℃~40℃,当换热冷凝器下端臭气排气口或臭气排气管内的温度传感器检测到臭气温度大于40℃时,检测控制装置输出控制信号打开换热冷凝器上端盖上方的臭气进气电磁阀,关闭旁通支路电磁阀,使臭气经换热冷凝器冷却后再进入生物除臭装置;而当换热冷凝器下端臭气排气口或臭气排气管内的温度传感器检测到臭气温度小于10℃时,检测控制装置输出控制信号关闭换热冷凝器上端盖上方的臭气进气电磁阀,打开旁通支路电磁阀,使臭气不进入换热冷凝器降温;检测控制装置通过温度传感器检测换热冷凝器的臭气排气温度,检测控制装置输出控制信号控制换热冷凝器的臭气进气电磁阀或旁通支路电磁阀,使生物除臭装置在10℃~40℃温度区间工作,既保证除臭效果,又避免生物除臭装置中微生物的休眠和死亡。Referring to FIG. 1, FIG. 2, FIG. 3 and FIG. 4, an odor heat exchange condensation system of the present invention comprises a heat exchange condenser, a temperature sensor, a biological deodorizing device, a detection control device, an odor collecting pipe and an odor. The exhaust pipe, the heat exchange condenser comprises an upper end cover, a tank body and a lower end cover which are sequentially connected, the upper end of the upper end cover has an odor air inlet flange, and the lower end of the odor collecting pipe is connected with the odor air inlet flange Fixed, the lower end of the lower end cover has an odor exhaust flange, the odor exhaust flange is connected with the odor exhaust pipe, the odor exhaust pipe is connected to the intake fan inlet, and the exhaust fan exhaust port is connected to the biological deodorization. a bypass branch and a bypass branch solenoid valve are connected between the odor collecting pipe and the inlet of the induced draft fan; a fresh air intake flange is arranged at a lower portion of the side wall of the heat exchanger condenser The upper part of the side wall of the heat exchange condenser is provided with a hot air exhaust flange, and the hot air exhaust flange is connected to the thermal energy load through the hot air induced draft fan and the hot air duct; the air exchange is installed in the tank of the heat exchange condenser Heater; odor gas is installed in the lower part of the odor collecting pipe The gas solenoid valve is provided with a temperature sensor in the odor exhaust port or the odor exhaust pipe at the lower end of the heat exchange condenser, and the output of the temperature sensor is connected to the signal input end of the detection control device, and the control signal outputted by the detection control device is connected to A stinky intake solenoid valve or a bypass branch solenoid valve, wherein the air heat exchanger installed in the heat exchange condenser tank is a tubular heat exchanger, and the specific structure is: installing a tube sheet on the upper part of the tank body, in the tank The lower tube plate is installed in the lower part of the body, and a plurality of air holes are evenly arranged on the upper tube plate and the lower tube plate, and the corresponding air holes of the upper tube plate and the lower tube plate are connected by a heat exchange tube, and the inner cavity of the heat exchange tube is connected with the odor, and the heat exchange tube The outer space is in communication with fresh air, and a plurality of tie rods are fixed on the lower tube sheet, and a plurality of trimmed partitions are evenly arranged in the space between the fresh air intake and the hot air exhaust in the tank, and the diameter of the partition is equal to The inner diameter of the tank body, the partition plate is fixedly fixed on the tie rod in the axial direction, and the lower end cover is The nozzle is connected to the water inlet of the U-shaped tube, the outlet position of the U-shaped tube is lower than the lower end cover, and the temperature control in the odor exhaust port or the odor exhaust pipe of the lower end of the heat exchange condenser set by the detection control device is controlled. The range is from 10 ° C to 40 ° C. When the temperature sensor in the odor exhaust port or the odor exhaust pipe of the lower end of the heat exchange condenser detects that the odor temperature is greater than 40 ° C, the detection control device outputs a control signal to open the upper end of the heat exchange condenser. The odor air intake solenoid valve above the cover closes the bypass branch solenoid valve, so that the odor gas is cooled by the heat exchange condenser and then enters the biological deodorization device; and when the odor gas exhaust port or odor at the lower end of the heat exchange condenser When the temperature sensor in the exhaust pipe detects that the odor temperature is less than 10 ° C, the detection control device outputs a control signal to close the odor air intake solenoid valve above the upper end cover of the heat exchange condenser, and opens the bypass branch solenoid valve to make the odor not Entering the heat exchange condenser to cool down; the detection control device detects the odor exhaust temperature of the heat exchange condenser through the temperature sensor, and the output control signal of the detection control device controls the odor inlet solenoid valve or the bypass branch electromagnetic of the heat exchange condenser The valve enables the biological deodorizing device to operate in a temperature range of 10 ° C to 40 ° C to ensure the deodorizing effect and avoid the dormancy and death of microorganisms in the biological deodorizing device.
一种臭气换热冷凝方法,包括:An odor heat exchange condensation method comprising:
(1)设计制造臭气换热冷凝器:臭气换热冷凝器包括依次连接固定的上端盖、罐体、下端盖;上端盖上端具有臭气进气法兰,臭气收集管道与臭气进气法兰连接固定,臭气收集管道下部安装有臭气进气电磁阀,下端盖底端具有臭气排气法兰,臭气排气法兰与臭气排气管道连接固定,换热冷凝器下端臭气排气口或臭气排气管道内安装有温度传感器,所述罐体内安装有空气换热器,在罐体侧壁上部设有热空气排气法兰,罐体侧壁下部设有新鲜空气进气法兰;(1) Design and manufacture of odor heat exchange condenser: odor heat exchange condenser includes upper end cover, tank body and lower end cover which are connected in turn; odor gas inlet flange, odor gas collection pipe and odor on upper end of upper end cover The intake flange is fixedly connected, and the odor gas intake solenoid valve is installed at the lower part of the odor collecting pipe, and the odor exhaust flange is provided at the bottom end of the lower end cover, and the odor exhaust flange is fixedly connected with the odor exhaust pipe, and the heat exchange is performed. A temperature sensor is installed in the odor exhaust port or the odor exhaust pipe at the lower end of the condenser, and an air heat exchanger is installed in the tank body, and a hot air exhaust flange is arranged on the upper side of the tank side wall, and the tank side wall is provided a fresh air intake flange is provided at the lower portion;
(2)连接臭气换热冷凝系统:换热冷凝器下端臭气排气口的温度传感器输出的模拟信号连接至检测控制装置输入端,检测控制装置输出的控制信号连接至臭气进气电磁阀或旁通支路电磁阀;臭气换热冷凝器下端连接的臭气排气管道与引风 机进气口连接,引风机排气口连接生物除臭装置,在臭气收集管道与引风机进气口之间还连接有旁通支路及旁通支路电磁阀;罐体侧壁下部的新鲜空气进气法兰为新鲜冷空气入口,而罐体侧壁上部的热空气排气法兰通过热空气引风机及热空气管道连接热能负载;在换热冷凝器下端盖出水口连接U型排水管;(2) Connecting the odor heat exchange condensation system: the analog signal output from the temperature sensor of the lower end of the heat exchange condenser is connected to the input end of the detection control device, and the control signal outputted by the detection control device is connected to the odor air intake electromagnetic Valve or bypass branch solenoid valve; odor exhaust pipe connected to the lower end of the odor heat exchange condenser The air inlet of the machine is connected, the exhaust port of the induced draft fan is connected with the biological deodorizing device, and the bypass branch and the bypass branch solenoid valve are connected between the odor collecting pipe and the inlet of the induced draft fan; the lower part of the side wall of the tank The fresh air intake flange is a fresh cold air inlet, and the hot air exhaust flange on the upper side of the tank side is connected to the thermal energy load through a hot air induced draft fan and a hot air duct; the water outlet connection U is connected to the lower end of the heat exchange condenser Type drain pipe;
(3)检测控制装置控制开启换热冷凝器的进气管道上的臭气进气电磁阀,启动引风机,臭气经臭气收集管道引入换热冷凝器的换热管内,启动热能负载前端的引风机,新鲜空气经新鲜空气进气口进入换热冷凝器的换热管外周,换热管内含热臭气与管外的新鲜空气在换热冷凝器内形成对流,通过换热管管壁进行充分的热交换;(3) The detection control device controls the odor gas intake solenoid valve on the intake pipe of the heat exchange condenser to be turned on, and the induced draft fan is started, and the odor gas is introduced into the heat exchange tube of the heat exchange condenser through the odor gas collection pipe, and the front end of the heat energy load is started. The induced draft fan, fresh air enters the outer circumference of the heat exchange tube of the heat exchange condenser through the fresh air inlet, and the hot odor in the heat exchange tube forms fresh convection with the fresh air outside the tube in the heat exchange condenser, and passes through the heat exchange tube The wall undergoes sufficient heat exchange;
(4)臭气经换热冷凝器换热、冷却后经臭气排气口排出,再经引风机引至生物除臭装置内,臭气经生物除臭装置吸收、转化,达标后排放;另外,将经换热冷凝器加热的新鲜空气从热空气排气口排出,引入热能负载中,为热能负载提供新鲜的热空气;(4) The odor gas is exchanged and exchanged by the heat exchange condenser, and then discharged through the odor exhaust port, and then introduced into the biological deodorizing device by the induced draft fan, and the odor is absorbed and converted by the biological deodorizing device, and discharged after reaching the standard; In addition, the fresh air heated by the heat exchange condenser is discharged from the hot air exhaust port and introduced into the thermal energy load to provide fresh hot air for the thermal energy load;
(5)臭气经换热冷凝器降温后产生的冷凝水汇集在换热冷凝器的下端盖中,当下端盖中的冷凝水液位达到一定值时,由于压差作用,冷凝水自动从U型管排水口排至沟渠中;(5) The condensed water generated by the odor gas cooled by the heat exchange condenser is collected in the lower end cover of the heat exchange condenser. When the condensed water level in the lower end cap reaches a certain value, the condensed water is automatically removed due to the pressure difference. The U-shaped pipe drain is discharged into the ditch;
(6)当换热冷凝器臭气排气口的温度传感器所检测的臭气温度大于40度时,检测控制装置输出控制信号打开换热冷凝器进气管道上的臭气进气电磁阀,关闭旁通支路电磁阀,使进入生物除臭滤装置的臭气在换热冷凝器内冷却;而当温度传感器所检测的臭气温度小于10度时,检测控制装置输出控制信号关闭换热冷凝器的臭气进气电磁阀,打开旁通支路电磁阀,使臭气不进入换热冷凝器内降温,使生物除臭装置在10℃至40℃温度区间工作,既保证除臭效果,又使生物除 臭装置中的微生物不至于休眠和死亡。(6) When the temperature of the odor detected by the temperature sensor of the odor outlet of the heat exchange condenser is greater than 40 degrees, the detection control device outputs a control signal to open the odor intake solenoid valve on the intake pipe of the heat exchange condenser, Closing the bypass branch solenoid valve, so that the odor entering the biological deodorizing filter device is cooled in the heat exchange condenser; and when the temperature of the odor detected by the temperature sensor is less than 10 degrees, the detection control device outputs a control signal to turn off the heat exchange The odor gas inlet solenoid valve of the condenser opens the bypass branch solenoid valve, so that the odor does not enter the heat exchanger condenser to cool down, so that the biological deodorizing device works in the temperature range of 10 ° C to 40 ° C, thereby ensuring the deodorizing effect. And let the creatures The microorganisms in the stinky device do not sleep and die.
下面结合附图,对本发明作进一步具体说明:The present invention will be further described in detail below with reference to the accompanying drawings:
本发明所涉及的换热冷凝器结构示意图如图2所示,换热冷凝器从上到下依次由上端盖101、上管板102、罐体111、下管板112、下端盖107和U型管113构成,上管板102和下管板112上均匀布置很多气孔,上管板102和下管板112对应气孔间用换热管103连接,在下管板112上固定多根拉杆105,且在空气进、出口之间错落、均匀地布置有多块切边的隔板104,隔板104固定在拉杆105上,隔板104的直径小于罐体111的内径,上端盖101上设置有臭气进气法兰109,下端盖107的上部设置有臭气排气法兰108,罐体111侧壁下部设置有冷空气进气法兰106,罐体111侧壁上部设置有热空气排气法兰110,U型管113的进水口固定在下端盖107的底部,U型管113的最高液位低于臭气排气法兰108的最低点。The schematic diagram of the heat exchange condenser according to the present invention is shown in FIG. 2. The heat exchange condenser is sequentially composed of an upper end cover 101, an upper tube sheet 102, a can body 111, a lower tube sheet 112, a lower end cover 107 and U from top to bottom. The tube 113 is formed, and a plurality of air holes are evenly arranged on the upper tube plate 102 and the lower tube plate 112. The upper tube plate 102 and the lower tube plate 112 are connected by a heat exchange tube 103 corresponding to the air holes, and a plurality of tie rods 105 are fixed on the lower tube plate 112. And a plurality of trimmed partitions 104 are arranged evenly between the air inlet and outlet, and the partition 104 is fixed on the pull rod 105. The diameter of the partition 104 is smaller than the inner diameter of the tank 111, and the upper end cover 101 is provided with The odor air intake flange 109, the upper end of the lower end cover 107 is provided with an odor exhaust flange 108, the lower part of the side wall of the tank body 111 is provided with a cold air intake flange 106, and the upper part of the side wall of the tank body 111 is provided with a hot air exhaust line The gas flange 110, the water inlet of the U-shaped tube 113 is fixed at the bottom of the lower end cover 107, and the highest liquid level of the U-shaped tube 113 is lower than the lowest point of the odor exhaust flange 108.
本发明所涉及的臭气换热冷凝方法示意图如图1所示,一种臭气换热冷凝装置及方法主要包括换热冷凝器202、电磁阀201A和201B、引风机203和205、热能负载204、生物除臭装置206、温度传感器207、检测控制装置208、以及臭气输送管道等,换热冷凝器202的臭气进气法兰109连接臭气收集管道,臭气排气法兰108经排气管道连接引风机205的进气口,在臭气排气口安装有温度传感器207,引风机205的排气口经管道连接生物除臭装置206的进气口,在换热冷凝器202进气管道上设置有电磁阀201A,并设有旁通支路,臭气换热冷凝器202旁通支路设置有电磁阀201B,换热冷凝器202的热空气排气法兰110经管道连接引风机203的进气口,引风机203的排气口经管道连接热能负载204的进气口。The schematic diagram of the odor heat exchange condensation method according to the present invention is shown in FIG. 1. An odor heat exchange condensing device and method mainly comprises a heat exchange condenser 202, electromagnetic valves 201A and 201B, induced draft fans 203 and 205, and thermal energy load. 204, the biological deodorizing device 206, the temperature sensor 207, the detecting and controlling device 208, and the odor conveying pipe, etc., the odor inlet flange 109 of the heat exchange condenser 202 is connected to the odor collecting pipe, and the odor exhausting flange 108 The air inlet of the induced draft fan 205 is connected via an exhaust duct, and a temperature sensor 207 is installed at the odor exhaust port, and the exhaust port of the induced draft fan 205 is connected to the air inlet of the biological deodorizing device 206 via a pipeline, in the heat exchange condenser The solenoid valve 201A is provided with a solenoid valve 201A, and a bypass branch is provided. The bypass branch of the odor heat exchange condenser 202 is provided with a solenoid valve 201B, and the hot air exhaust flange 110 of the heat exchange condenser 202 is The pipe is connected to the intake port of the induced draft fan 203, and the exhaust port of the induced draft fan 203 is connected to the intake port of the thermal energy load 204 via a pipe.
本发明的臭气换热冷凝方法中,所述步骤(3)—(6)结合附图具体描述如下: In the odor heat exchange condensation method of the present invention, the steps (3)-(6) are specifically described below with reference to the accompanying drawings:
(3)检测控制装置控制208开启臭气换热冷凝器的进气管道上的电磁阀201A,启动引风机205,臭气经臭气进气法兰109引入换热冷凝器202的换热管103内,启动热能负载204前段的引风机203,新鲜空气经新鲜空气进气法兰106进入换热冷凝器202的换热管103外,换热管103内含热臭气与换热管103管外的新鲜空气在换热冷凝器202内形成对流,通过换热管202管壁进行充分地热交换;(3) The detection control device control 208 opens the electromagnetic valve 201A on the intake pipe of the odor heat exchange condenser, activates the induced draft fan 205, and the odor is introduced into the heat exchange tube of the heat exchange condenser 202 via the odor inlet flange 109. In the 103, the induced draft fan 203 of the front stage of the thermal energy load 204 is started, and the fresh air enters the heat exchange tube 103 of the heat exchange condenser 202 via the fresh air intake flange 106, and the heat exchange tube 103 contains the hot odor and the heat exchange tube 103. The fresh air outside the tube forms convection in the heat exchange condenser 202, and is fully heat exchanged through the tube wall of the heat exchange tube 202;
(4)臭气经换热冷凝器202换热、冷却后经臭气排气法兰108排出,再经生物除臭装置206的进气口引至生物除臭装置206内,臭气经生物除臭装置206吸收、转化,达标后排放;将经换热冷凝器202加热的空气从热空气排气法兰110排出,经引风机203引入热能负载204中,为热能负载204提供新鲜的热空气;(4) The odor is exchanged and exchanged by the heat exchange condenser 202, and then discharged through the odor exhaust flange 108, and then introduced into the biological deodorizing device 206 through the air inlet of the biological deodorizing device 206, and the odor is passed through the living body. The deodorizing device 206 absorbs, converts, and discharges after reaching the standard; the air heated by the heat exchange condenser 202 is discharged from the hot air exhaust flange 110, introduced into the thermal energy load 204 via the induced draft fan 203, and provides fresh heat to the thermal energy load 204. air;
(5)臭气经换热冷凝器202降温后产生的冷凝水汇集在换热冷凝器202的下端盖107中,当下端盖107中的冷凝水液位达到一定值时,由于压差作用,冷凝水自动从U型管113排水口排至沟渠中;(5) The condensed water generated after the odor is cooled by the heat exchange condenser 202 is collected in the lower end cover 107 of the heat exchange condenser 202. When the condensed water level in the lower end cover 107 reaches a certain value, due to the pressure difference, The condensate is automatically discharged from the U-tube 113 drain to the ditch;
(6)当检测控制装置208检测安装在换热冷凝器202臭气排气口的温度传感器207检测到臭气温度大于40度时,检测控制装置208打开臭气换热冷凝器202的进气管道上的电磁阀201A,关闭旁通支路电磁阀201B,使进入生物除臭装置206的臭气经臭气换热冷凝器202冷却;而当检测控制装置208检测安装在换热冷凝器202臭气排气口的温度传感器207检测到生物除臭装置206内除臭填料的温度小于10度时,控制系统208关闭换热冷凝器202的进气管道上的电磁阀201A,打开旁通支路电磁阀201B,使臭气不进入换热冷凝器202降温,使生物除臭装置206在10℃~40℃温度区间工作,既保证除臭效果,又使生物除臭装置206中的微生物不至于休眠和死亡。 (6) When the detection control device 208 detects that the temperature sensor 207 installed in the odor exhaust port of the heat exchange condenser 202 detects that the odor temperature is greater than 40 degrees, the detection control device 208 opens the intake of the odor heat exchange condenser 202. The solenoid valve 201A on the pipe closes the bypass branch solenoid valve 201B, so that the odor entering the biological deodorizing device 206 is cooled by the odor heat exchange condenser 202; and when the detecting control device 208 detects the installation in the heat exchange condenser 202 When the temperature sensor 207 of the odor exhaust port detects that the temperature of the deodorizing filler in the biological deodorizing device 206 is less than 10 degrees, the control system 208 turns off the solenoid valve 201A on the intake pipe of the heat exchange condenser 202, and opens the bypass branch. The road electromagnetic valve 201B prevents the odor from entering the heat exchange condenser 202 to cool down, so that the biological deodorizing device 206 operates in the temperature range of 10 ° C to 40 ° C, thereby ensuring the deodorizing effect and preventing the microorganisms in the biological deodorizing device 206 from being As for dormancy and death.

Claims (6)

  1. 一种臭气换热冷凝系统,其特征在于:包括换热冷凝器、温度传感器、生物除臭装置、检测控制装置、臭气收集管道和臭气排气管道,所述的换热冷凝器包括依次连接固定的上端盖、罐体、下端盖,上端盖的上端具有臭气进气法兰,臭气收集管道下端与臭气进气法兰连接固定,下端盖的下端具有臭气排气法兰,臭气排气法兰与臭气排气管道连接固定,臭气排气管道连接引风机进气口,引风机排气口连接生物除臭装置;在臭气收集管道与引风机进气口之间还连接有旁通支路及旁通支路电磁阀;所述换热冷凝器的罐体侧壁下部设有新鲜空气进气法兰,换热冷凝器的罐体侧壁上部设有热空气排气法兰,热空气排气法兰通过热空气引风机及热空气管道连接热能负载;在换热冷凝器的罐体内安装空气换热器;臭气收集管道下部安装有臭气进气电磁阀,在换热冷凝器下端臭气排气口或臭气排气管道内安装有温度传感器,温度传感器的输出连接检测控制装置的信号输入端,而检测控制装置输出的控制信号连接臭气进气电磁阀或旁通支路电磁阀。An odor heat exchange condensation system, comprising: a heat exchange condenser, a temperature sensor, a biological deodorizing device, a detection control device, an odor collecting pipe and an odor exhaust pipe, wherein the heat exchange condenser comprises The fixed upper end cover, the can body and the lower end cover are sequentially connected, and the upper end of the upper end cover has an odor air inlet flange, the lower end of the odor collecting pipe is fixedly connected with the odor air inlet flange, and the lower end of the lower end cover has an odor exhausting method. Lan, the odor exhaust flange is connected with the odor exhaust pipe, the odor exhaust pipe is connected to the intake fan inlet, the exhaust fan exhaust port is connected to the biological deodorizing device; the odor collecting pipe and the induced draft fan are used for intake A bypass branch and a bypass branch solenoid valve are also connected between the ports; a fresh air intake flange is arranged at a lower portion of the side wall of the heat exchanger condenser, and a top wall of the tank body of the heat exchange condenser is provided There is a hot air exhaust flange, the hot air exhaust flange is connected to the thermal energy load through the hot air induced draft fan and the hot air duct; the air heat exchanger is installed in the tank of the heat exchange condenser; the odor is installed in the lower part of the odor collecting pipeline Intake solenoid valve, in heat exchange A temperature sensor is installed in the odor exhaust port or the odor exhaust pipe at the lower end of the condenser, and the output of the temperature sensor is connected to the signal input end of the detection control device, and the control signal outputted by the detection control device is connected to the odor intake solenoid valve or the side. Tongzhi Road solenoid valve.
  2. 根据权利要求1所述的一种臭气换热冷凝系统,其特征在于:所述换热冷凝器罐体内安装的空气换热器为列管式热交换器,具体结构为:在罐体内上部安装上管板,在罐体内下部安装下管板,上管板上和下管板上均匀布置很多气孔,上管板和下管板的对应气孔间用换热管连接,换热管内腔与臭气连通,换热管外侧空间与新鲜空气连通。The odor heat exchange condensation system according to claim 1, wherein the air heat exchanger installed in the heat exchange condenser tank is a tubular heat exchanger, and the specific structure is: in the upper part of the tank body. The upper tube sheet is installed, and the lower tube sheet is installed in the lower part of the tank body, and a plurality of air holes are evenly arranged on the upper tube plate and the lower tube plate, and the corresponding air holes of the upper tube plate and the lower tube plate are connected by heat exchange tubes, and the inner tube of the heat exchange tube is The odor is connected, and the outer space of the heat exchange tube is connected with fresh air.
  3. 根据权利要求1所述的一种臭气换热冷凝系统,其特征在于:在下管板上固定多根拉杆,在罐体内的新鲜空气进气和热空气排气之间的空间内均匀布置有多块切边的隔板,隔板沿罐体轴线方向错落地固定在拉杆上。An odor heat exchange condensation system according to claim 1, wherein a plurality of tie rods are fixed on the lower tube sheet, and are uniformly arranged in a space between the fresh air intake and the hot air exhaust in the tank body. A plurality of trimmed partitions are fixed on the tie rods in the direction of the axis of the tank.
  4. 根据权利要求1所述的一种臭气换热冷凝系统,其特征在于:所述的下端 盖出水口连接U型管的进水口,U型管的排水口位置低于下端盖,U型管的最高液位低于臭气排气法兰的最低点。An odor heat exchange condensation system according to claim 1, wherein said lower end The water outlet is connected to the water inlet of the U-shaped tube, and the outlet position of the U-shaped tube is lower than the lower end cover, and the highest liquid level of the U-shaped tube is lower than the lowest point of the odor-exhaust flange.
  5. 一种臭气换热冷凝方法,其特征在于:包括:An odor heat exchange condensation method, characterized in that:
    (1)设计制造臭气换热冷凝器:臭气换热冷凝器包括依次连接固定的上端盖、罐体、下端盖;上端盖上端具有臭气进气法兰,臭气收集管道与臭气进气法兰连接固定,臭气收集管道下部安装有臭气进气电磁阀,下端盖底端具有臭气排气法兰,臭气排气法兰与臭气排气管道连接固定,换热冷凝器下端臭气排气口或臭气排气管道内安装有温度传感器,所述罐体内安装有空气换热器,在罐体侧壁上部设有热空气排气法兰,罐体侧壁下部设有新鲜空气进气法兰;(1) Design and manufacture of odor heat exchange condenser: odor heat exchange condenser includes upper end cover, tank body and lower end cover which are connected in turn; odor gas inlet flange, odor gas collection pipe and odor on upper end of upper end cover The intake flange is fixedly connected, and the odor gas intake solenoid valve is installed at the lower part of the odor collecting pipe, and the odor exhaust flange is provided at the bottom end of the lower end cover, and the odor exhaust flange is fixedly connected with the odor exhaust pipe, and the heat exchange is performed. A temperature sensor is installed in the odor exhaust port or the odor exhaust pipe at the lower end of the condenser, and an air heat exchanger is installed in the tank body, and a hot air exhaust flange is arranged on the upper side of the tank side wall, and the tank side wall is provided a fresh air intake flange is provided at the lower portion;
    (2)连接臭气换热冷凝系统:换热冷凝器下端臭气排气口的温度传感器输出的模拟信号连接至检测控制装置输入端,检测控制装置输出的控制信号连接至臭气进气电磁阀或旁通支路电磁阀;臭气换热冷凝器下端连接的臭气排气管道与引风机进气口连接,引风机排气口连接生物除臭装置,在臭气收集管道与引风机进气口之间还连接有旁通支路及旁通支路电磁阀;罐体侧壁下部的新鲜空气进气法兰为新鲜冷空气入口,而罐体侧壁上部的热空气排气法兰通过热空气引风机及热空气管道连接热能负载;在换热冷凝器下端盖出水口连接U型排水管;(2) Connecting the odor heat exchange condensation system: the analog signal output from the temperature sensor of the lower end of the heat exchange condenser is connected to the input end of the detection control device, and the control signal outputted by the detection control device is connected to the odor air intake electromagnetic Valve or bypass branch solenoid valve; the odor gas exhaust pipe connected to the lower end of the odor heat exchange condenser is connected with the inlet of the induced draft fan, and the exhaust fan exhaust port is connected to the biological deodorizing device, and the odor collecting pipe and the induced draft fan A bypass branch and a bypass branch solenoid valve are also connected between the air inlets; a fresh air intake flange at a lower portion of the side wall of the tank is a fresh cold air inlet, and a hot air exhaust method at the upper side of the tank side wall The blue is connected to the thermal energy load through the hot air induced draft fan and the hot air pipe; the U-shaped drain pipe is connected to the lower end of the heat exchange condenser;
    (3)检测控制装置控制开启换热冷凝器的进气管道上的臭气进气电磁阀,启动引风机,臭气经臭气收集管道引入换热冷凝器的换热管内,启动热能负载前端的引风机,新鲜空气经新鲜空气进气口进入换热冷凝器的换热管外周,换热管内含热臭气与管外的新鲜空气在换热冷凝器内形成对流,通过换热管管壁进行充分的热交换;(3) The detection control device controls the odor gas intake solenoid valve on the intake pipe of the heat exchange condenser to be turned on, and the induced draft fan is started, and the odor gas is introduced into the heat exchange tube of the heat exchange condenser through the odor gas collection pipe, and the front end of the heat energy load is started. The induced draft fan, fresh air enters the outer circumference of the heat exchange tube of the heat exchange condenser through the fresh air inlet, and the hot odor in the heat exchange tube forms fresh convection with the fresh air outside the tube in the heat exchange condenser, and passes through the heat exchange tube The wall undergoes sufficient heat exchange;
    (4)臭气经换热冷凝器换热、冷却后经臭气排气口排出,再经引风机引至生 物除臭装置内,臭气经生物除臭装置吸收、转化,达标后排放;另外,将经换热冷凝器加热的新鲜空气从热空气排气口排出,引入热能负载中,为热能负载提供新鲜的热空气;(4) The odor is exchanged by the heat exchange condenser, cooled, discharged through the odor exhaust port, and then introduced to the living by the induced draft fan. In the deodorizing device, the odor is absorbed and converted by the biological deodorizing device, and is discharged after reaching the standard; in addition, the fresh air heated by the heat exchange condenser is discharged from the hot air exhaust port and introduced into the thermal energy load to provide the thermal energy load. Fresh hot air;
    (5)臭气经换热冷凝器降温后产生的冷凝水汇集在换热冷凝器的下端盖中,当下端盖中的冷凝水液位达到一定值时,由于压差作用,冷凝水自动从U型管排水口排至沟渠中;(5) The condensed water generated by the odor gas cooled by the heat exchange condenser is collected in the lower end cover of the heat exchange condenser. When the condensed water level in the lower end cap reaches a certain value, the condensed water is automatically removed due to the pressure difference. The U-shaped pipe drain is discharged into the ditch;
    (6)当检测控制装置检测到安装在换热冷凝器臭气排气口的温度传感器所检测的臭气温度大于40度时,检测控制装置输出控制信号打开换热冷凝器进气管道上的臭气进气电磁阀,关闭旁通支路电磁阀,使进入生物除臭滤装置的臭气在换热冷凝器内冷却;而当检测控制装置检测到安装在换热冷凝器臭气排气口的温度传感器所检测的臭气温度小于10度时,检测控制装置输出控制信号关闭换热冷凝器的臭气收集管道上的电磁阀,打开旁通支路电磁阀,使臭气不进入换热冷凝器内降温,使生物除臭装置在10℃至40℃温度区间工作,既保证除臭效果,又使生物除臭装置中的微生物不至于休眠和死亡;(6) When the detection control device detects that the temperature of the odor detected by the temperature sensor installed in the odor outlet of the heat exchange condenser is greater than 40 degrees, the detection control device outputs a control signal to open the intake pipe of the heat exchange condenser. The odor air intake electromagnetic valve closes the bypass branch solenoid valve, so that the odor entering the biological deodorizing filter device is cooled in the heat exchange condenser; and when the detecting control device detects the odor exhaust installed in the heat exchange condenser When the temperature of the odor detected by the temperature sensor of the mouth is less than 10 degrees, the detection control device outputs a control signal to close the electromagnetic valve on the odor collecting pipe of the heat exchange condenser, and opens the electromagnetic valve of the bypass branch to prevent the odor from entering. The temperature in the thermal condenser is lowered, so that the biological deodorizing device operates in a temperature range of 10 ° C to 40 ° C, which not only ensures the deodorizing effect, but also prevents the microorganisms in the biological deodorizing device from sleeping and dying;
  6. 根据权利要求5所述的一种臭气换热冷凝方法,其特征在于:所述的检测控制装置设定的换热冷凝器下端臭气排气口或臭气排气管道内的温度控制范围为10℃~40℃,当换热冷凝器下端臭气排气口或臭气排气管内的温度传感器检测到臭气温度大于40℃时,检测控制装置输出控制信号打开换热冷凝器上端盖上方的臭气进气电磁阀,关闭旁通支路电磁阀,使臭气经换热冷凝器冷却后再进入生物除臭装置;而当换热冷凝器下端臭气排气口或臭气排气管内的温度传感器检测到臭气温度小于10℃时,检测控制装置输出控制信号关闭换热冷凝器上端盖上方的臭气进气电磁阀,打开旁通支路电磁阀,使臭气不进入换热冷凝器降温;检测 控制装置通过温度传感器检测换热冷凝器的臭气排气温度,检测控制装置输出控制信号控制换热冷凝器的臭气进气电磁阀或旁通支路电磁阀,使生物除臭装置在10℃~40℃温度区间工作,既保证除臭效果,又避免生物除臭装置中微生物的休眠和死亡。 The odor heat exchange condensation method according to claim 5, characterized in that: the temperature control range in the odor exhaust port or the odor exhaust pipe of the lower end of the heat exchange condenser set by the detecting control device 10 ° C ~ 40 ° C, when the temperature sensor at the lower end of the heat exchanger condenser or the temperature sensor in the odor exhaust pipe detects that the odor temperature is greater than 40 ° C, the detection control device outputs a control signal to open the upper end cap of the heat exchange condenser The upper odor air intake solenoid valve closes the bypass branch solenoid valve, so that the odor gas is cooled by the heat exchange condenser and then enters the biological deodorization device; and when the odor exhaust port or the odor line at the lower end of the heat exchange condenser When the temperature sensor in the trachea detects that the odor temperature is less than 10 °C, the detection control device outputs a control signal to close the odor air intake solenoid valve above the upper end cover of the heat exchange condenser, and opens the bypass branch solenoid valve to prevent the odor from entering. Heat exchange condenser cooling; detection The control device detects the odor exhaust temperature of the heat exchange condenser through the temperature sensor, and the detection control device outputs a control signal to control the odor inlet solenoid valve or the bypass branch solenoid valve of the heat exchange condenser, so that the biological deodorizing device is at 10 Working in the temperature range of °C ~ 40 °C, not only to ensure the deodorization effect, but also to avoid the dormancy and death of microorganisms in the biological deodorization device.
PCT/CN2016/090669 2016-07-11 2016-07-20 Odorous gas heat-exchange condensation system and method WO2018010197A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201610538030.7 2016-07-11
CN201610538030.7A CN106839796A (en) 2016-07-11 2016-07-11 A kind of foul smell heat exchange condensing system and method

Publications (1)

Publication Number Publication Date
WO2018010197A1 true WO2018010197A1 (en) 2018-01-18

Family

ID=59145268

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2016/090669 WO2018010197A1 (en) 2016-07-11 2016-07-20 Odorous gas heat-exchange condensation system and method

Country Status (2)

Country Link
CN (1) CN106839796A (en)
WO (1) WO2018010197A1 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110013732A (en) * 2019-04-29 2019-07-16 黑龙江华泽农牧发展有限公司 Crouch rotating waste fermentation closed cycle fixed nitrogen deodoration system
CN111253026B (en) * 2020-03-23 2023-10-31 湖南屎壳郎环境科技有限公司 Automatic dewatering and heat cyclic utilization's high temperature aerobic fermentation system
CN111253027B (en) * 2020-03-23 2023-11-03 湖南屎壳郎环境科技有限公司 Automatic dewatering and heat cyclic utilization's high temperature aerobic fermentation system
CN111558609A (en) * 2020-05-08 2020-08-21 河北乾蓝环保工程有限公司 Kitchen waste fermentation heating oxygen supply process and device
CN111790212A (en) * 2020-07-23 2020-10-20 中农新科(苏州)有机循环研究院有限公司 Waste gas recycling system for organic waste biological drying process

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101284208A (en) * 2007-12-28 2008-10-15 青海洁神食品垃圾处理产业有限公司 Kitchen rubbish high temperature organic exhaust gas integration biological treatment device and process
CN201625431U (en) * 2010-02-05 2010-11-10 海南金海浆纸业有限公司 Anti-odor pollution device in pulping vacuum evaporation plant
CN103341309A (en) * 2013-07-19 2013-10-09 烟台润达垃圾处理环保股份有限公司 Technology for processing damp and hot foul gas
CN104888592A (en) * 2015-06-23 2015-09-09 河南博奥皮业有限公司 Method and system for deodorizing tannery wastewater
CN105289231A (en) * 2015-10-19 2016-02-03 江苏奥琳斯邦热能设备有限公司 Waste gas treatment system
CN105498523A (en) * 2015-12-11 2016-04-20 天紫工程管理(天津)有限公司 Waste gas treatment system

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2302406Y (en) * 1997-06-16 1998-12-30 郎逵 Air pre-heater with node heat-exchange tube
JP2011152526A (en) * 2010-01-28 2011-08-11 Gunma Prefecture Adsorption tower equipped with flow passage for heating medium feeding and use of the adsorption tower
CN204485644U (en) * 2015-02-10 2015-07-22 广东生益科技股份有限公司 A kind of gas cleaning plant
CN105642083A (en) * 2016-04-05 2016-06-08 湖南景翌湘台环保高新技术开发有限公司 Combined treatment technology for biochemical odors
CN206146226U (en) * 2016-07-11 2017-05-03 湖南屎壳郎环境科技有限公司 Foul smell heat transfer condensing system

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101284208A (en) * 2007-12-28 2008-10-15 青海洁神食品垃圾处理产业有限公司 Kitchen rubbish high temperature organic exhaust gas integration biological treatment device and process
CN201625431U (en) * 2010-02-05 2010-11-10 海南金海浆纸业有限公司 Anti-odor pollution device in pulping vacuum evaporation plant
CN103341309A (en) * 2013-07-19 2013-10-09 烟台润达垃圾处理环保股份有限公司 Technology for processing damp and hot foul gas
CN104888592A (en) * 2015-06-23 2015-09-09 河南博奥皮业有限公司 Method and system for deodorizing tannery wastewater
CN105289231A (en) * 2015-10-19 2016-02-03 江苏奥琳斯邦热能设备有限公司 Waste gas treatment system
CN105498523A (en) * 2015-12-11 2016-04-20 天紫工程管理(天津)有限公司 Waste gas treatment system

Also Published As

Publication number Publication date
CN106839796A (en) 2017-06-13

Similar Documents

Publication Publication Date Title
WO2018010197A1 (en) Odorous gas heat-exchange condensation system and method
WO2018010196A1 (en) System and method for livestock and poultry farm odor and flue gas treatment
WO2018010192A1 (en) Solid high-temperature aerobic fermentation reaction system and method
WO2021189742A1 (en) Horizontal aerobic fermentation reactor and waste heat utilization water removal system
CN110013732A (en) Crouch rotating waste fermentation closed cycle fixed nitrogen deodoration system
CN202212406U (en) Garbage treatment device for cyclically utilizing organisms to dry secondary pollutants
CN208907086U (en) Household composting device
CN110773549A (en) Efficient energy-saving system of organic garbage biological treatment machine
CN207958268U (en) A kind of pressurization reverse-flow type organic waste gasification furnace
CN210907370U (en) Organic refuse treatment waste heat recovery device
CN108911802A (en) Household composting device
CN206777550U (en) A kind of bactericidal unit
WO2016061847A1 (en) Method for facilitating aerobic fermentation reaction using combustion waste gas
CN113233927A (en) Composting device and composting method for organic garbage
CN111790212A (en) Waste gas recycling system for organic waste biological drying process
CN115789627B (en) High-efficient burning tail gas processing apparatus of biomass energy
CN206229201U (en) A kind of livestock and poultry farm foul smell smoke gas treatment system
CN206146226U (en) Foul smell heat transfer condensing system
CN205619297U (en) High -efficient garbage incinerator's gas circulation device
CN217921868U (en) Composting device for organic garbage
CN206156995U (en) Good oxygen mummification device of city domestic sewage excess sludge
CN206139007U (en) High -efficiency biological filler deodorizing device
CN209669082U (en) Crouch rotating waste fermentation deodoration system in situ
CN207006175U (en) A kind of film anhydration system using waste incineration residual heat of exhaust flue gas desiccation rubbish
CN219907428U (en) Kitchen waste fermentation box based on ultra-high temperature aerobic composting technology

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 16908522

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 16908522

Country of ref document: EP

Kind code of ref document: A1