CN113898960B - Complementary system of gas-liquid furnace and regenerative incinerator for waste gas treatment and use method thereof - Google Patents
Complementary system of gas-liquid furnace and regenerative incinerator for waste gas treatment and use method thereof Download PDFInfo
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- CN113898960B CN113898960B CN202111111160.XA CN202111111160A CN113898960B CN 113898960 B CN113898960 B CN 113898960B CN 202111111160 A CN202111111160 A CN 202111111160A CN 113898960 B CN113898960 B CN 113898960B
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- 239000002912 waste gas Substances 0.000 title claims abstract description 43
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- 230000001172 regenerating effect Effects 0.000 title claims description 17
- 238000005406 washing Methods 0.000 claims abstract description 36
- 238000012423 maintenance Methods 0.000 claims abstract description 7
- 239000007789 gas Substances 0.000 claims description 161
- 238000001514 detection method Methods 0.000 claims description 101
- 230000002265 prevention Effects 0.000 claims description 30
- 238000011084 recovery Methods 0.000 claims description 23
- 239000010815 organic waste Substances 0.000 claims description 19
- 238000012545 processing Methods 0.000 claims description 17
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- 238000012544 monitoring process Methods 0.000 claims description 10
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 7
- 239000003546 flue gas Substances 0.000 claims description 7
- 230000001105 regulatory effect Effects 0.000 claims description 6
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/04—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste liquors, e.g. sulfite liquors
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/50—Control or safety arrangements
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
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- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Incineration Of Waste (AREA)
Abstract
The invention discloses a complementary system for a gas-liquid furnace and a heat accumulating type incinerator for waste gas treatment and a use method thereof, comprising a remote monitoring device, a gas-liquid incinerator, a pre-washing tower and a heat accumulating type incinerator, wherein an air outlet pipe of the gas-liquid incinerator and an air outlet pipe of the heat accumulating type incinerator are respectively communicated with an air inlet of the pre-washing tower through electromagnetic control fireproof valves, and one side of the air outlet pipe of the gas-liquid incinerator and one side of the air outlet pipe of the heat accumulating type incinerator are respectively communicated with one end of an explosion-proof main control pipe through electromagnetic control explosion-proof three-way valves; the technology for performing seamless switching is effectively designed, so that various manual and time losses caused by temporary shutdown maintenance are avoided, and seamless linkage is realized through switching of two systems of the gas-liquid incinerator and the heat accumulating type incinerator; the two sets of systems are really realized to be mutually standby, and seamless switching is realized; ensure the stable production of enterprises.
Description
Technical Field
The invention relates to the technical field of treatment of tail end waste gas in medical chemical industry, in particular to a complementary system of a gas-liquid furnace and a regenerative incinerator for waste gas treatment and a use method thereof.
Background
With the development of global economy and the acceleration of urban process, the discharge of industrial wastewater and waste gas is increased, the pollution is serious, and the organic wastewater containing BOD >100mg/L, COD >2000mg/L is commonly called high-concentration organic waste liquid. These waste solutions often have one or more of the deleterious characteristics of flammability, corrosiveness, acute toxicity, leaching toxicity, reactivity, infectivity, carcinogenicity, teratogenicity, mutagenicity, etc. Common methods for treating organic waste liquid are solvent extraction, membrane separation, oxidation, adsorption III and incineration. Wherein, the solvent extraction method, the membrane separation method, the oxidation method and the adsorption method are difficult to thoroughly eliminate the harm of organic waste liquid and easily cause secondary pollution.
In addition, the emission of VOCs in China mainly comes from fixed source combustion, road traffic solvent product use and industrial processes. Among the many man-made sources, industrial sources are the main sources of VOCs pollution, and have the characteristics of concentrated emission, high emission intensity, high concentration and complex components. The harm of VOCs to the human body is mainly twofold: one is that the harmful components directly affect the health of human bodies, and the two VOCs can form PM2.5 precursors, so that the health of human bodies is indirectly affected. According to the principle of generating VOCs in the atmosphere and the physicochemical properties of VOCs, the control technology can be divided into two main types, namely process control and end control. The process control is aimed at the production process of VOCs, and the generation of VOCs is reduced in principle, and is generally realized through process lifting, technical transformation and leakage control. The tail end control aims at the chemical characteristics of the VOCs, is applied to the treatment of the exhaust gas of the VOCs, and controls the emission of the VOCs by using methods such as combustion, decomposition and the like. At present, the waste liquid is treated by an incineration method at home and abroad, incineration equipment of waste gas is various, and different furnace types can be adopted for different industrial waste liquids and waste gas.
The gas-liquid incinerator is mainly used for treating liquid waste which can be conveyed by a pump. A simple structure, typically a refractory lined cylinder (horizontally or vertically placed), is fitted with one or more burners. The principle is that waste gas and waste liquid are burnt directly through nozzle to be atomized into fine liquid drops, and the fine liquid drops are burnt in suspension state in a high-temperature flame area, the burning temperature is controlled to be about 1000-1150 ℃, the highest temperature cannot exceed 1200 ℃, and the lowest temperature cannot be lower than 900 ℃. The temperature of the burned flue gas can be recycled through a waste heat boiler to generate steam, the temperature of the flue gas is reduced from 1100 ℃ to about 300 ℃ after the flue gas is recycled, and the lowest temperature cannot be lower than 280 ℃.
The heat accumulating incinerator (RTO) waste gas treating apparatus is one kind of efficient organic waste gas treating apparatus. Compared with the traditional catalytic combustion and direct combustion type thermal oxidation furnace (TO), the catalytic combustion and direct combustion type thermal oxidation furnace has the characteristics of high thermal efficiency (more than or equal TO 95%), low running cost, capability of treating waste gas with high air quantity, medium and low concentration, and the like, and can also perform secondary waste heat recovery when the concentration is slightly high, so that the production running cost is greatly reduced. The main working principle of RTO is to heat the organic waste gas to 760 ℃ or higher, so that VOCs in the waste gas are oxidized and decomposed into carbon dioxide and water. The high-temperature gas generated by oxidation flows through a special ceramic heat accumulator to heat the ceramic body to store heat, and the heat is used for preheating organic waste gas which enters subsequently. Thereby saving fuel consumption for exhaust gas warming. The ceramic regenerators should be divided into more than two (including two), each regenerator being subjected to the procedures of heat accumulation, heat release, cleaning, etc. in turn.
According to different local environmental protection policies, a plurality of parks and factories are required to use 2 sets of RTO systems to completely treat the discharged waste gas, so that the investment cost is greatly increased; in addition, the RTO can treat the waste gas after heating for about four hours under the condition that continuous working conditions cannot be achieved, and if the RTO adopts a hot standby system to assist in heat standby, the heating energy consumption of the system can be greatly increased. In addition, the waste gas of chemical industry and pharmaceutical industry is often various in variety, and enterprises are difficult to solve all waste gas in the field by using one incinerator.
Disclosure of Invention
The invention provides a complementary system of a gas-liquid furnace and a regenerative incinerator for waste gas treatment.
The scheme of the invention is as follows:
The system comprises a remote monitoring system, a gas-liquid incinerator, a pre-washing tower and a heat accumulating type incinerator, wherein the remote monitoring system comprises a pressure detection unit, a temperature detection unit, a concentration detection unit, a treatment control display unit and a control unit, the gas-liquid incinerator and the heat accumulating type incinerator are respectively provided with the pressure detection unit, the temperature detection unit, the concentration detection unit and the control unit, the pressure detection unit, the concentration detection unit and the temperature detection unit detect information and are transmitted to the treatment control display unit, the treatment control display unit controls the control unit, the control unit comprises a control device for controlling each switch electromagnetic control fireproof valve, an electromagnetic control explosion-proof three-way valve switch controller, a gas-liquid incinerator controller and a heat accumulating type incinerator, an air outlet pipe of the gas-liquid incinerator is respectively communicated with an air inlet of the pre-washing tower through an electromagnetic control fireproof valve, one side of the air outlet pipe of the gas-liquid incinerator is respectively communicated with one side of the air outlet pipe of the heat accumulating type incinerator through an electromagnetic control three-way valve and one side of an explosion-proof main control pipe, and one side of the other side of the main control pipe of the heat accumulating type incinerator is respectively communicated with one side of the exhaust gas inlet pipe of the exhaust gas of the heat accumulating type incinerator; the electromagnetic control fire-proof valve is arranged on the exhaust gas inlet pipe from the exhaust gas inlet pipe side pipe of the gas-liquid incinerator to the exhaust gas inlet pipe between the gas-liquid incinerator, and the electromagnetic control fire-proof valve is arranged on the exhaust gas inlet pipe from the exhaust gas pipe from the side pipe of the heat accumulating type incinerator to the exhaust gas inlet pipe between the heat accumulating type incinerator.
As an optimized technical scheme, the temperature detection unit comprises an in-furnace temperature detection device and a flue gas temperature detection device, the concentration detection unit is an organic concentration detector, the pressure detection unit is a pressure transmitter, the processing control display unit comprises a display, a processor and an information writing device, the processor respectively receives information detected by the temperature detection unit, the concentration detection unit and the pressure detection unit, the processor processes detection information data and transmits the detection information data to the display to provide the display for operators, the information writing device is in control connection with the control unit through the processor, the operators input information instructions through the information writing device and send the information instructions to the control unit through the processor, and accordingly the opening and closing of each electromagnetic control fireproof valve and the electromagnetic control anti-explosion three-way valve and the opening and closing of the electromagnetic control anti-explosion three-way valve are controlled through the control unit.
As the preferable technical scheme, the pre-washing tower further comprises a recovery tank, a recovery tank and a liquid extracting pump, wherein the recovery tank is arranged at the bottom of the pre-washing tower, the recovery tank is communicated with the liquid extracting pump through the recovery tank, the liquid extracting pump is respectively communicated with a spray pipe and a drain pipe of the pre-washing tower through a three-way valve, and a concentration detector is further arranged on an air outlet pipe of the pre-washing tower.
As a preferable technical scheme, the concentration detection unit further comprises an exhaust gas concentration detector, wherein the exhaust gas concentration detector is positioned on an air outlet pipe of the pre-washing tower and is used for detecting that the exhaust gas of the pre-washing tower meets the elimination standard.
As the preferable technical scheme, three ends of the explosion-proof three-way pipe are respectively communicated with the explosion-proof main control pipe, a side pipe of an exhaust gas inlet pipe of the gas-liquid incinerator and a side pipe of an exhaust gas inlet pipe of the heat accumulating type incinerator through electromagnetic control fireproof valves.
As the preferable technical scheme, the recovery tank is provided with a medicament feeding device.
The invention also discloses a method for using the complementary system of the gas-liquid furnace and the regenerative incinerator for waste gas treatment,
The gas-liquid incinerator and the heat accumulating type incinerator are used for respectively incinerating waste gas, the incinerated gas is sprayed through a pre-washing tower and then discharged after being detected to be qualified, and the electromagnetic control explosion-proof three-way valve is in a closed state and the electromagnetic control fireproof valve on the three ends of the explosion-proof three-way pipe is in a closed state;
When the gas-liquid incinerator needs to be overhauled and the gas-liquid incinerator is still incinerating organic waste gas, the pressure and the temperature in the gas-liquid incinerator and the pressure in the heat accumulating type incinerator are monitored by remote monitoring, when the pressure and the temperature in the gas-liquid incinerator and the heat accumulating type incinerator are inconsistent, a gas-liquid incinerator controller and a heat accumulating type incinerator controller in a control unit are controlled by a treatment control display unit, the temperature and the pressure of the gas-liquid incinerator and the heat accumulating type incinerator tend to be consistent, then the gas-liquid incinerator is closed, an electromagnetic control fireproof valve at the connection end of an electromagnetic control explosion-proof three-way valve and the gas-liquid incinerator and an explosion-proof main control pipe is opened, an electromagnetic control fireproof valve at the connection position of the explosion-proof main control pipe and the explosion-proof three-way pipe is opened, the electromagnetic control fireproof valve at the connection position of the explosion-proof three-way pipe and the exhaust gas inlet pipe side pipe of the heat accumulating type incinerator is opened, the electromagnetic control fireproof valve on the exhaust gas inlet pipe between the gas inlet pipe side pipe of the gas liquid incinerator and the gas liquid incinerator is closed by a treatment control display unit, the electromagnetic control fireproof valve on the gas-liquid incinerator outlet pipe is closed, and the electromagnetic control valve on the gas inlet pipe of the gas-liquid incinerator is closed, and the electromagnetic control fireproof valve on the air inlet pipe is closed after the temperature and the pressure of the heat accumulating type incinerator is detected to reach the normal condition, and the electromagnetic control valve is connected to the electromagnetic control valve, and the electromagnetic control valve is closed, and the electromagnetic control valve is connected to the electromagnetic valve and has the normal concentration control and has the normal concentration and has the control and has the advantages; then, an electromagnetic control fireproof valve is opened at the joint of the explosion-proof three-way pipe and a side pipe of one side of an exhaust gas inlet pipe of the gas-liquid incinerator, an maintainer overhauls the gas-liquid incinerator equipment rapidly, and organic exhaust gas to be combusted, which is incinerated by the gas-liquid incinerator, is connected into the inlet pipe of the heat accumulating type incinerator through the side pipe of one side of the exhaust gas inlet pipe of the gas-liquid incinerator to continue the exhaust gas combustion operation;
When the heat accumulating type incinerator is in fault or overhauled, the temperature and pressure parameters in the gas-liquid incinerator and the heat accumulating type incinerator are also regulated in the same way, the gas-liquid incinerator controller and the heat accumulating type incinerator controller in the control unit are controlled by processing the control display unit, so that the temperature and pressure of the gas-liquid incinerator and the heat accumulating type incinerator tend to be consistent, then the heat accumulating type incinerator is closed, the two ends of the electromagnetic control explosion-proof three-way valve connected with the heat accumulating type incinerator and the explosion-proof main control pipe are opened, the electromagnetic control fireproof valve at the communication part of the explosion-proof main control pipe and the explosion-proof three-way pipe is opened, the electromagnetic control fireproof valve at the communication part of the explosion-proof three-way pipe and the side pipe of the exhaust gas inlet pipe of the gas-liquid incinerator is opened, the electromagnetic control fire prevention valve on the exhaust gas inlet pipe of the heat accumulating type incinerator is closed from a side pipe on one side of the exhaust gas inlet pipe of the heat accumulating type incinerator to the exhaust gas inlet pipe between the heat accumulating type incinerators, the electromagnetic control fire prevention valve on the exhaust pipe of the heat accumulating type incinerator is closed, the exhaust gas to be treated in the heat accumulating type incinerator is led into the gas-liquid incinerator which normally operates in a switching valve mode to be incinerated, when the information sent by the concentration detection unit, the pressure detection unit and the temperature detection unit which are arranged in the heat accumulating type incinerator is processed by the processing control display unit and then fed back to an operator, and after the temperature, the pressure and the concentration of the exhaust gas reach the access standards of maintenance personnel, the electromagnetic control fire prevention valve at the connection position of the electromagnetic control fire prevention three-way valve, the heat accumulating type incinerator and the explosion prevention main pipe is controlled to be closed; then, an electromagnetic control fireproof valve on the joint of the explosion-proof three-way pipe and the side pipe of the exhaust gas inlet pipe of the heat accumulating type incinerator is opened, an maintainer overhauls the equipment of the heat accumulating type incinerator quickly, and the organic exhaust gas to be burnt, which is burnt by the heat accumulating type incinerator, is connected into the gas inlet pipe of the gas-liquid incinerator through the side pipe of the exhaust gas inlet pipe of the heat accumulating type incinerator to continue the exhaust gas combustion.
As the preferable technical scheme, when the gas-liquid incinerator incinerates the waste gas containing hydrogen, the electromagnetic control explosion-proof three-way valve is in a closed state, and the electromagnetic control fire-proof valve on the three ends of the explosion-proof three-way pipe is in a closed state.
As the preferable technical scheme, the air inlet pipe of the gas-liquid incinerator is communicated with a high-concentration organic waste gas source, and the air inlet pipe of the heat accumulating type incinerator is communicated with a low-concentration organic waste gas source.
Due to the adoption of the technical scheme.
The invention has the advantages that:
The technology for performing seamless switching is effectively designed, so that various manual and time losses caused by temporary shutdown maintenance are avoided, and seamless linkage is realized through switching of two systems of the gas-liquid incinerator and the heat accumulating type incinerator;
the repeated investment is reduced, if the factory has an exhaust gas furnace or a gas-liquid incinerator, the investment of a set of standby RTO system can be reduced, and the investment is saved by more than millions of yuan.
The two sets of systems are really realized to be mutually standby, and seamless switching is realized; ensuring the stable production of enterprises;
The effective process design is subjected to seamless switching, so that the two systems can be communicated when necessary, the waste water and waste gas in a factory can be completely and effectively treated, the cost for investing another set of RTO system can be saved, and the gas-liquid incinerator can also transmit waste heat to the RTO system, thereby realizing the maximization of energy utilization. Generally, the low-concentration waste gas can adopt an RTO heat accumulating incinerator, the high-concentration VOC waste gas can adopt a gas-liquid incinerator, and an RTO system can also be adopted, because the RTO heat accumulating incinerator is equivalent to heating the waste gas to 70-90 ℃, and the gas-liquid direct combustion furnace is required to heat the waste gas to 260-280 ℃, for low-concentration organic waste gas, the RTO is obviously more economical than the gas-liquid incinerator, so that the RTO incinerator and the gas-liquid incinerator are combined, the heat value of the waste gas can be improved, the fuel cost and the investment cost can be reduced, and meanwhile, the waste gas pollution in a factory is completely treated.
Drawings
FIG. 1 is a process flow diagram of an embodiment of the present invention;
FIG. 2 is a frame diagram of a pre-wash column in accordance with an embodiment of the invention.
1-A gas-liquid incinerator; 2-a heat accumulating type incinerator; 3-a pre-wash column; 4-a pressure detection unit; 5-a temperature detection unit; a 6-concentration detection unit; 7-processing the control display unit; 8-a controller for electromagnetically controlling the fireproof valve; 9-a gas-liquid incinerator controller; 10-a regenerative incinerator controller; 13-an electromagnetic control explosion-proof three-way valve switch controller; 14-electromagnetic control fire damper; 15-electromagnetic control three-way valve; 16-an explosion-proof main control pipe; 17-explosion-proof three-way pipe; 60-concentration detector.
Detailed Description
In order to overcome the defects, the invention provides a complementary system of a gas-liquid furnace for waste gas treatment and a regenerative incinerator, which solves the problems in the background technology.
The system comprises a remote monitoring system, a gas-liquid incinerator, a pre-washing tower and a heat accumulating type incinerator, wherein the remote monitoring system comprises a pressure detection unit, a temperature detection unit, a concentration detection unit, a treatment control display unit and a control unit, the gas-liquid incinerator and the heat accumulating type incinerator are respectively provided with the pressure detection unit, the temperature detection unit, the concentration detection unit and the control unit, the pressure detection unit, the concentration detection unit and the temperature detection unit detect information and are transmitted to the treatment control display unit, the treatment control display unit controls the control unit, the control unit comprises a control device for controlling each switch electromagnetic control fireproof valve, an electromagnetic control explosion-proof three-way valve switch controller, a gas-liquid incinerator controller and a heat accumulating type incinerator, an air outlet pipe of the gas-liquid incinerator is respectively communicated with an air inlet of the pre-washing tower through an electromagnetic control fireproof valve, one side of the air outlet pipe of the gas-liquid incinerator is respectively communicated with one side of the air outlet pipe of the heat accumulating type incinerator through an electromagnetic control three-way valve and one side of an explosion-proof main control pipe, and one side of the other side of the main control pipe of the heat accumulating type incinerator is respectively communicated with one side of the exhaust gas inlet pipe of the exhaust gas of the heat accumulating type incinerator; the electromagnetic control fire-proof valve is arranged on the exhaust gas inlet pipe from the exhaust gas inlet pipe side pipe of the gas-liquid incinerator to the exhaust gas inlet pipe between the gas-liquid incinerator, and the electromagnetic control fire-proof valve is arranged on the exhaust gas inlet pipe from the exhaust gas pipe from the side pipe of the heat accumulating type incinerator to the exhaust gas inlet pipe between the heat accumulating type incinerator.
The temperature detection unit comprises temperature detection equipment and flue gas temperature detection equipment in the furnace, the concentration detection unit is an organic concentration detector, the pressure detection unit is a pressure transmitter, the processing control display unit comprises a display, a processor and information writing equipment, the processor receives information detected by the temperature detection unit, the concentration detection unit and the pressure detection unit respectively, the processor processes detection information data and transmits the detection information data to the display for providing to operators, the information writing equipment is in control connection with the control unit through the processor, the operators input information instructions through the information writing equipment and send the information instructions to the control unit through the processor, and accordingly the opening and closing of each electromagnetic control fireproof valve and the electromagnetic control explosion-proof three-way valve and the opening and closing of the gas-liquid incinerator and the heat accumulating incinerator are controlled through the control unit.
The pre-washing tower further comprises a recovery tank, a recovery tank and a liquid suction pump, the recovery tank is arranged at the bottom of the pre-washing tower and is communicated with the liquid suction pump through the recovery tank, the liquid suction pump is respectively communicated with a spray pipe and a drain pipe of the pre-washing tower through a three-way valve, and a concentration detector is further arranged on an air outlet pipe of the pre-washing tower.
The concentration detection unit further comprises an exhaust gas concentration detector, wherein the exhaust gas concentration detector is positioned on an air outlet pipe of the pre-washing tower and is used for detecting that the exhaust gas of the pre-washing tower meets the elimination standard.
And three ends of the explosion-proof three-way pipe are respectively communicated with the explosion-proof main control pipe, the side pipe of the exhaust gas inlet pipe of the gas-liquid incinerator and the side pipe of the exhaust gas inlet pipe of the heat accumulating type incinerator through electromagnetic control fireproof valves.
And the recovery tank is provided with a medicament feeding device.
The invention also discloses a method for using the complementary system of the gas-liquid furnace and the regenerative incinerator for waste gas treatment,
The gas-liquid incinerator and the heat accumulating type incinerator are used for respectively incinerating waste gas, the incinerated gas is sprayed through a pre-washing tower and then discharged after being detected to be qualified, and the electromagnetic control explosion-proof three-way valve is in a closed state and the electromagnetic control fireproof valve on the three ends of the explosion-proof three-way pipe is in a closed state;
When the gas-liquid incinerator needs to be overhauled and the gas-liquid incinerator is still incinerating organic waste gas, the pressure and the temperature in the gas-liquid incinerator and the pressure in the heat accumulating type incinerator are monitored by remote monitoring, when the pressure and the temperature in the gas-liquid incinerator and the heat accumulating type incinerator are inconsistent, a gas-liquid incinerator controller and a heat accumulating type incinerator controller in a control unit are controlled by a treatment control display unit, the temperature and the pressure of the gas-liquid incinerator and the heat accumulating type incinerator tend to be consistent, then the gas-liquid incinerator is closed, an electromagnetic control fireproof valve at the connection end of an electromagnetic control explosion-proof three-way valve and the gas-liquid incinerator and an explosion-proof main control pipe is opened, an electromagnetic control fireproof valve at the connection position of the explosion-proof main control pipe and the explosion-proof three-way pipe is opened, the electromagnetic control fireproof valve at the connection position of the explosion-proof three-way pipe and the exhaust gas inlet pipe side pipe of the heat accumulating type incinerator is opened, the electromagnetic control fireproof valve on the exhaust gas inlet pipe between the gas inlet pipe side pipe of the gas liquid incinerator and the gas liquid incinerator is closed by a treatment control display unit, the electromagnetic control fireproof valve on the gas-liquid incinerator outlet pipe is closed, and the electromagnetic control valve on the gas inlet pipe of the gas-liquid incinerator is closed, and the electromagnetic control fireproof valve on the air inlet pipe is closed after the temperature and the pressure of the heat accumulating type incinerator is detected to reach the normal condition, and the electromagnetic control valve is connected to the electromagnetic control valve, and the electromagnetic control valve is closed, and the electromagnetic control valve is connected to the electromagnetic valve and has the normal concentration control and has the normal concentration and has the control and has the advantages; then, an electromagnetic control fireproof valve is opened at the joint of the explosion-proof three-way pipe and a side pipe of one side of an exhaust gas inlet pipe of the gas-liquid incinerator, an maintainer overhauls the gas-liquid incinerator equipment rapidly, and organic exhaust gas to be combusted, which is incinerated by the gas-liquid incinerator, is connected into the inlet pipe of the heat accumulating type incinerator through the side pipe of one side of the exhaust gas inlet pipe of the gas-liquid incinerator to continue the exhaust gas combustion operation;
When the heat accumulating type incinerator is in fault or overhauled, the temperature and pressure parameters in the gas-liquid incinerator and the heat accumulating type incinerator are also regulated in the same way, the gas-liquid incinerator controller and the heat accumulating type incinerator controller in the control unit are controlled by processing the control display unit, so that the temperature and pressure of the gas-liquid incinerator and the heat accumulating type incinerator tend to be consistent, then the heat accumulating type incinerator is closed, the two ends of the electromagnetic control explosion-proof three-way valve connected with the heat accumulating type incinerator and the explosion-proof main control pipe are opened, the electromagnetic control fireproof valve at the communication part of the explosion-proof main control pipe and the explosion-proof three-way pipe is opened, the electromagnetic control fireproof valve at the communication part of the explosion-proof three-way pipe and the side pipe of the exhaust gas inlet pipe of the gas-liquid incinerator is opened, the electromagnetic control fire prevention valve on the exhaust gas inlet pipe of the heat accumulating type incinerator is closed from a side pipe on one side of the exhaust gas inlet pipe of the heat accumulating type incinerator to the exhaust gas inlet pipe between the heat accumulating type incinerators, the electromagnetic control fire prevention valve on the exhaust pipe of the heat accumulating type incinerator is closed, the exhaust gas to be treated in the heat accumulating type incinerator is led into the gas-liquid incinerator which normally operates in a switching valve mode to be incinerated, when the information sent by the concentration detection unit, the pressure detection unit and the temperature detection unit which are arranged in the heat accumulating type incinerator is processed by the processing control display unit and then fed back to an operator, and after the temperature, the pressure and the concentration of the exhaust gas reach the access standards of maintenance personnel, the electromagnetic control fire prevention valve at the connection position of the electromagnetic control fire prevention three-way valve, the heat accumulating type incinerator and the explosion prevention main pipe is controlled to be closed; then, an electromagnetic control fireproof valve on the joint of the explosion-proof three-way pipe and the side pipe of the exhaust gas inlet pipe of the heat accumulating type incinerator is opened, an maintainer overhauls the equipment of the heat accumulating type incinerator quickly, and the organic exhaust gas to be burnt, which is burnt by the heat accumulating type incinerator, is connected into the gas inlet pipe of the gas-liquid incinerator through the side pipe of the exhaust gas inlet pipe of the heat accumulating type incinerator to continue the exhaust gas combustion.
When the gas-liquid incinerator incinerates waste gas containing hydrogen, the electromagnetic control explosion-proof three-way valve is in a closed state, and the electromagnetic control fireproof valve on the three ends of the explosion-proof three-way pipe is in a closed state.
The air inlet pipe of the gas-liquid incinerator is communicated with a high-concentration organic waste gas source, and the air inlet pipe of the heat accumulating type incinerator is communicated with a low-concentration organic waste gas source.
The invention is further described in connection with the following embodiments in order to make the technical means, the creation features, the achievement of the purpose and the effect of the invention easy to understand.
Examples
The complementary system of the gas-liquid furnace and the heat accumulating type incinerator for treating the waste gas comprises a remote monitoring device, a gas-liquid incinerator 1, a pre-washing tower 3 and a heat accumulating type incinerator 2, wherein the remote monitoring device comprises a pressure detection unit 4, a temperature detection unit 5, a concentration detection unit 6, a treatment control display unit 7 and a control unit, the gas-liquid incinerator 1 and the heat accumulating type incinerator 2 are respectively provided with the pressure detection unit 4, the temperature detection unit 5, the concentration detection unit 6 and the control unit, the pressure detection unit 4, the concentration detection unit 6 and the temperature detection unit 5 detect information and transmit the information to the treatment control display unit 7, the treatment control display unit 7 controls the control unit, the control unit comprises a control device 8 for controlling each switch electromagnetic control fireproof valve, an electromagnetic control explosion-proof three-way valve switch controller 13, a gas-liquid incinerator controller 9 and a heat accumulating type incinerator controller 10, an air outlet pipe of the gas-liquid incinerator 1 and an air outlet pipe of the heat accumulating type incinerator 2 are respectively communicated with an air inlet of the pre-washing tower 2 through a control fireproof valve 14, one side of the gas-liquid incinerator 1 and one side of the heat accumulating type incinerator 2 are respectively communicated with one side of an explosion-proof pipe 16 of the main control pipe of the waste gas pipe 16 and one side of the other side of the heat accumulating type incinerator 2; an electromagnetic control fireproof valve 14 is arranged between a side pipe of an exhaust gas inlet pipe of the gas-liquid incinerator 1 and the exhaust gas inlet pipe between the gas-liquid incinerator 1, and an electromagnetic control fireproof valve 14 is arranged between a side pipe of an inlet pipe of the heat accumulating type incinerator 2 and the exhaust gas inlet pipe between the heat accumulating type incinerator 2. The electromagnetic control explosion-proof three-way valve switch controller 13 controls the switch of the electromagnetic control explosion-proof three-way valve 15, and the controller 8 of the electromagnetic control fireproof valve controls the individual switch of each electromagnetic control fireproof valve 14.
The temperature detection unit 5 comprises an in-furnace temperature detection device and a flue gas temperature detection device, the concentration detection unit 6 is an organic concentration detector, the pressure detection unit 4 is a pressure transmitter, the processing control display unit 7 comprises a display, a processor and an information writing device, the processor respectively receives information detected by the temperature detection unit 5, the concentration detection unit 6 and the pressure detection unit 4, and the processor processes detection information data and transmits the detection information data to the display to provide the display for operators, so that the operators can know the in-furnace pressure, the in-furnace temperature, the in-furnace exhaust gas concentration, the out-furnace exhaust gas concentration, the temperature gradient of the output exhaust gas after the exhaust gas is burnt, and the temperature difference and the pressure difference between the gas-liquid incinerator 1 and the heat accumulating type incinerator 2; the information writing device is in control connection with the control unit through the processor, an operator inputs information instructions through the information writing device and sends the information instructions to the control unit through the processor, so that the opening and closing of each electromagnetic control fireproof valve 14 and the electromagnetic control explosion-proof three-way valve 15 are controlled through the control unit, the gas-liquid incinerator 1 and the heat accumulating type incinerator 2 are regulated and controlled, the waste gas inlet amount of the gas-liquid incinerator 1 and the heat accumulating type incinerator 2 can be regulated and controlled, the opening and closing are carried out, the air inlet amount of the fan is controlled, and the information writing device comprises a keyboard and a mouse.
The pre-washing tower 3 further comprises a recovery tank, a recovery tank and a liquid pumping pump, the recovery tank is arranged at the bottom of the pre-washing tower, the recovery tank is communicated with the liquid pumping pump through the recovery tank, the liquid pumping pump is respectively communicated with a spray pipe and a sewage pipe of the pre-washing tower through a three-way valve, and a concentration detector 60 is further arranged on an air outlet pipe of the pre-washing tower.
The concentration detection unit 6 further comprises an exhaust gas concentration detector, which is located on the gas outlet pipe of the pre-scrubber 1 and is used for detecting that the exhaust gas of the pre-scrubber 1 meets the exclusion criteria.
Three ends of the explosion-proof three-way pipe 17 are respectively communicated with the explosion-proof main control pipe 16, the side pipe of the exhaust gas inlet pipe of the gas-liquid incinerator 1 and the side pipe of the exhaust gas inlet pipe of the heat accumulating type incinerator 2 through electromagnetic control fireproof valves 14.
And the recovery tank is provided with a medicament feeding device.
The using method comprises the following steps:
The gas-liquid incinerator 1 and the heat accumulating type incinerator 2 are used for respectively incinerating waste gas, the incinerated gas is sprayed through the pre-washing tower 3 and then discharged after being detected to be qualified, the electromagnetic control explosion-proof three-way valve 15 is in a closed state, and the electromagnetic control fireproof valves 14 on the three ends of the explosion-proof three-way pipe 17 are in a closed state;
When the gas-liquid incinerator 1 needs to be overhauled and the gas-liquid incinerator 1 is used for incinerating organic waste gas, the pressure and the temperature in the gas-liquid incinerator 1 and the heat accumulating type incinerator 2 are monitored and controlled by remote monitoring, when the temperature in the gas-liquid incinerator 1 and the heat accumulating type incinerator 2 is inconsistent, the gas-liquid incinerator controller 9 and the heat accumulating type incinerator controller 10 in the control unit are controlled by processing the control display unit 7, the temperature and the pressure of the gas-liquid incinerator 1 and the heat accumulating type incinerator 2 tend to be consistent, then the gas-liquid incinerator 1 is closed, the two ends of the connection of the electromagnetic control explosion-proof three-way valve 15 and the gas-liquid incinerator 1 and the explosion-proof main control pipe 16 are opened, the electromagnetic control fireproof valve 14 at the connection part of the explosion-proof main control pipe 16 and the explosion-proof three-way pipe 17 is opened, the electromagnetic control fireproof valve 14 at the connection part of the three-way pipe 17 and the side pipe of the waste gas inlet pipe of the heat accumulating type incinerator 2 is opened, the electromagnetic control fire prevention valve 14 on the exhaust gas inlet pipe side pipe of the gas-liquid incinerator 1 is closed to the electromagnetic control fire prevention valve 14 on the exhaust gas inlet pipe between the gas-liquid incinerators 1, the electromagnetic control fire prevention valve 14 on the gas outlet pipe of the gas-liquid incinerator 1 is closed, the exhaust gas to be treated in the gas-liquid incinerator 1 is led into the heat accumulating type incinerator 2 which operates normally to be incinerated in a switching valve mode, when the information sent by the concentration detection unit 6, the pressure detection unit 4 and the temperature detection unit 5 which are arranged in the gas-liquid incinerator 1 is processed by the processing control display unit 7 and then fed back to operators, after the temperature, the pressure and the exhaust gas concentration reach the access standards of the overhaulers, the two ends of the electromagnetic control explosion prevention three-way valve 15 connected with the gas-liquid incinerator 1 and the explosion prevention main control pipe 16 are controlled to be closed, closing the electromagnetic control fire valve 14 at the communication position of the explosion-proof main control pipe 16 and the explosion-proof three-way pipe 17; then, an electromagnetic control fireproof valve 14 is opened at the joint of the explosion-proof three-way pipe 17 and a side pipe of the exhaust gas inlet pipe of the gas-liquid incinerator 1, an maintainer overhauls the equipment of the gas-liquid incinerator 1 quickly, and organic exhaust gas to be combusted, which is combusted by the gas-liquid incinerator 1, is connected into the inlet pipe of the heat accumulating type incinerator 2 through the side pipe of the exhaust gas inlet pipe of the gas-liquid incinerator 1 to continue the exhaust gas combustion operation;
When the heat accumulating type incinerator 2 fails or overhauls, the temperature and pressure parameters in the gas-liquid incinerator 1 and the heat accumulating type incinerator 2 are regulated in the same way, the gas-liquid incinerator controller 9 and the heat accumulating type incinerator controller 10 in the control unit are controlled by the processing control display unit 7, so that the temperature and pressure of the gas-liquid incinerator 1 and the heat accumulating type incinerator 2 tend to be consistent, then the heat accumulating type incinerator 2 is closed, the two ends of the electromagnetic control explosion-proof three-way valve 15 connected with the heat accumulating type incinerator 2 and the explosion-proof main control pipe 16 are opened, the electromagnetic control fireproof valve 14 at the position where the explosion-proof main control pipe 16 is communicated with the explosion-proof three-way pipe 17 is opened, the electromagnetic control fireproof valve 14 at the position where the explosion-proof three-way pipe 17 is communicated with the side pipe of the exhaust gas inlet pipe of the gas-liquid incinerator 1 is opened, the electromagnetic control fire prevention valve on the exhaust gas inlet pipe side pipe of the heat accumulating type incinerator 2 is closed 14, the electromagnetic control fire prevention valve 14 on the exhaust gas outlet pipe of the heat accumulating type incinerator 2 is closed, the exhaust gas to be treated in the heat accumulating type incinerator 2 is led into the gas-liquid incinerator 1 which normally operates in a switching valve mode to be incinerated, when the information sent by the concentration detection unit 6, the pressure detection unit 4 and the temperature detection unit 5 which are arranged in the heat accumulating type incinerator 2 is processed by the processing control display unit 7 and then fed back to an operator, and after the temperature, the pressure and the exhaust gas concentration reach the access standards of maintenance personnel, the electromagnetic control fire prevention valve 14 at the connection position of the electromagnetic control fire prevention three-way valve 15 and the heat accumulating type incinerator 2 and the explosion prevention main control pipe 16 is controlled to be closed; then, an electromagnetic control fireproof valve 14 is opened at the joint of the explosion-proof three-way pipe 17 and the side pipe of the exhaust gas inlet pipe of the thermal storage type incinerator 2, an maintainer overhauls the equipment of the thermal storage type incinerator 2 quickly, and the organic exhaust gas to be burnt, which is burnt by the thermal storage type incinerator 2, is connected into the gas inlet pipe of the gas-liquid incinerator 1 through the side pipe of the exhaust gas inlet pipe of the thermal storage type incinerator 2 to continue the exhaust gas combustion.
When the gas-liquid incinerator 1 incinerates waste gas containing hydrogen, the electromagnetic control explosion-proof three-way valve 15 is closed, and the electromagnetic control fireproof valves 14 on the three ends of the explosion-proof three-way pipe 17 are closed.
The air inlet pipe of the gas-liquid incinerator 1 is communicated with a high-concentration organic waste gas source, and the air inlet pipe of the heat accumulating type incinerator 2 is communicated with a low-concentration organic waste gas source.
The foregoing has shown and described the basic principles, main features and advantages of the present invention. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, and that the above embodiments and descriptions are merely illustrative of the principles of the present invention, and various changes and modifications may be made without departing from the spirit and scope of the invention, which is defined in the appended claims. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (9)
1. A complementary system of a gas-liquid furnace and a regenerative incinerator for waste gas treatment, which is characterized in that:
The system comprises a remote monitoring unit, a gas-liquid incinerator, a pre-washing tower and a heat accumulating type incinerator, wherein the remote monitoring unit comprises a pressure detection unit, a temperature detection unit, a concentration detection unit, a treatment control display unit and a control unit, the gas-liquid incinerator and the heat accumulating type incinerator are respectively provided with the pressure detection unit, the temperature detection unit, the concentration detection unit and the control unit, the pressure detection unit, the concentration detection unit and the temperature detection unit detect information to be transmitted to the treatment control display unit, the treatment control display unit controls the control unit, the control unit comprises a controller for controlling electromagnetic control fireproof valves, an electromagnetic control explosion-proof three-way valve on-off controller, a gas-liquid incinerator controller and a heat accumulating type incinerator controller, an air outlet pipe of the gas-liquid incinerator and an air outlet pipe of the heat accumulating type incinerator are respectively communicated with an air inlet of the pre-washing tower through electromagnetic control fireproof valves, one side of the air outlet pipe of the gas-liquid incinerator and one side of the air outlet pipe of the gas-liquid incinerator are respectively communicated with one side of an explosion-proof main through electromagnetic control explosion-proof three-way valve, and one side of the exhaust gas side of the heat accumulating type main respectively; the electromagnetic control fire-proof valve is arranged on the exhaust gas inlet pipe from the exhaust gas inlet pipe side pipe of the gas-liquid incinerator to the exhaust gas inlet pipe between the gas-liquid incinerator, and the electromagnetic control fire-proof valve is arranged on the exhaust gas inlet pipe from the exhaust gas pipe from the side pipe of the heat accumulating type incinerator to the exhaust gas inlet pipe between the heat accumulating type incinerator.
2. The complementary system for a gas-liquid furnace and a regenerative incinerator for treating exhaust gas according to claim 1, wherein: the temperature detection unit comprises temperature detection equipment and flue gas temperature detection equipment in the furnace, the concentration detection unit is an organic concentration detector, the pressure detection unit is a pressure transmitter, the processing control display unit comprises a display, a processor and information writing equipment, the processor receives information detected by the temperature detection unit, the concentration detection unit and the pressure detection unit respectively, the processor processes detection information data and transmits the detection information data to the display for providing to operators, the information writing equipment is in control connection with the control unit through the processor, the operators input information instructions through the information writing equipment and send the information instructions to the control unit through the processor, and accordingly the opening and closing of each electromagnetic control fireproof valve and the electromagnetic control explosion-proof three-way valve and the opening and closing of the gas-liquid incinerator and the heat accumulating incinerator are controlled through the control unit.
3. The complementary system for a gas-liquid furnace and a regenerative incinerator for treating exhaust gas according to claim 1, wherein: the pre-washing tower further comprises a recovery tank, a recovery tank and a liquid suction pump, the recovery tank is arranged at the bottom of the pre-washing tower and is communicated with the liquid suction pump through the recovery tank, the liquid suction pump is respectively communicated with a spray pipe and a drain pipe of the pre-washing tower through a three-way valve, and a concentration detector is further arranged on an air outlet pipe of the pre-washing tower.
4. A complementary system for a gas-liquid furnace and a regenerative incinerator for treating exhaust gas according to claim 1 or 3, wherein: the concentration detection unit further comprises an exhaust gas concentration detector, wherein the exhaust gas concentration detector is positioned on an air outlet pipe of the pre-washing tower and is used for detecting that the exhaust gas of the pre-washing tower meets the elimination standard.
5. The complementary system for a gas-liquid furnace and a regenerative incinerator for treating exhaust gas according to claim 1, wherein: and three ends of the explosion-proof three-way pipe are respectively communicated with the explosion-proof main control pipe, the side pipe of the exhaust gas inlet pipe of the gas-liquid incinerator and the side pipe of the exhaust gas inlet pipe of the heat accumulating type incinerator through electromagnetic control fireproof valves.
6. A complementary system for a gas-liquid furnace and a regenerative incinerator for treating exhaust gas according to claim 3, wherein: and the recovery tank is provided with a medicament feeding device.
7. A method of using the complementary system of a gas-liquid furnace and a regenerative incinerator for treating exhaust gas according to claim 1,2 or 5, wherein:
The gas-liquid incinerator and the heat accumulating type incinerator are used for respectively incinerating waste gas, the incinerated gas is sprayed through a pre-washing tower and then discharged after being detected to be qualified, and the electromagnetic control explosion-proof three-way valve is in a closed state and the electromagnetic control fireproof valve on the three ends of the explosion-proof three-way pipe is in a closed state;
When the gas-liquid incinerator needs to be overhauled and the gas-liquid incinerator is still incinerating organic waste gas, the pressure and the temperature in the gas-liquid incinerator and the heat accumulating type incinerator are monitored by remote monitoring, when the pressure and the temperature in the gas-liquid incinerator and the heat accumulating type incinerator are inconsistent, the gas-liquid incinerator controller and the heat accumulating type incinerator controller in the control unit are controlled by the processing control display unit, so that the temperature and the pressure of the gas-liquid incinerator and the heat accumulating type incinerator tend to be consistent, then the gas-liquid incinerator is closed, the two ends of the electromagnetic control explosion-proof three-way valve connected with the gas-liquid incinerator and the explosion-proof main control pipe are opened, the electromagnetic control fireproof valve at the communication part of the explosion-proof main control pipe and the explosion-proof three-way pipe is opened, the electromagnetic control fireproof valve at the communication part of the explosion-proof three-way pipe and the side pipe of the waste gas inlet pipe of the heat accumulating type incinerator is opened, the electromagnetic control fire prevention valve on the exhaust gas inlet pipe of the gas-liquid incinerator is closed from a side pipe on one side of the exhaust gas inlet pipe of the gas-liquid incinerator to the exhaust gas inlet pipe of the gas-liquid incinerator, the electromagnetic control fire prevention valve on the exhaust pipe of the gas-liquid incinerator is closed, the exhaust gas to be treated in the gas-liquid incinerator is led into the heat accumulating type incinerator which operates normally to be incinerated in a switching valve mode, when the information sent by the concentration detection unit, the pressure detection unit and the temperature detection unit which are arranged in the gas-liquid incinerator is processed by the processing control display unit and then fed back to an operator, after the temperature, the pressure and the concentration of the exhaust gas reach the access standards of maintenance personnel, the electromagnetic control fire prevention valve at the connection position of the electromagnetic control fire prevention three-way valve, the gas-liquid incinerator and the explosion prevention main pipe is controlled to be closed; then, an electromagnetic control fireproof valve is opened at the joint of the explosion-proof three-way pipe and a side pipe of one side of an exhaust gas inlet pipe of the gas-liquid incinerator, an maintainer overhauls the gas-liquid incinerator equipment rapidly, and organic exhaust gas to be combusted, which is incinerated by the gas-liquid incinerator, is connected into the inlet pipe of the heat accumulating type incinerator through the side pipe of one side of the exhaust gas inlet pipe of the gas-liquid incinerator to continue the exhaust gas combustion operation;
When the heat accumulating type incinerator is in fault or overhauled, the temperature and pressure parameters in the gas-liquid incinerator and the heat accumulating type incinerator are also regulated in the same way, the gas-liquid incinerator controller and the heat accumulating type incinerator controller in the control unit are controlled by processing the control display unit, so that the temperature and pressure of the gas-liquid incinerator and the heat accumulating type incinerator tend to be consistent, then the heat accumulating type incinerator is closed, the two ends of the electromagnetic control explosion-proof three-way valve connected with the heat accumulating type incinerator and the explosion-proof main control pipe are opened, the electromagnetic control fireproof valve at the communication part of the explosion-proof main control pipe and the explosion-proof three-way pipe is opened, the electromagnetic control fireproof valve at the communication part of the explosion-proof three-way pipe and the side pipe of the exhaust gas inlet pipe of the gas-liquid incinerator is opened, the electromagnetic control fire prevention valve on the exhaust gas inlet pipe of the heat accumulating type incinerator is closed from a side pipe on one side of the exhaust gas inlet pipe of the heat accumulating type incinerator to the exhaust gas inlet pipe between the heat accumulating type incinerators, the electromagnetic control fire prevention valve on the exhaust pipe of the heat accumulating type incinerator is closed, the exhaust gas to be treated in the heat accumulating type incinerator is led into the gas-liquid incinerator which normally operates in a switching valve mode to be incinerated, when the information sent by the concentration detection unit, the pressure detection unit and the temperature detection unit which are arranged in the heat accumulating type incinerator is processed by the processing control display unit and then fed back to an operator, and after the temperature, the pressure and the concentration of the exhaust gas reach the access standards of maintenance personnel, the electromagnetic control fire prevention valve at the connection position of the electromagnetic control fire prevention three-way valve, the heat accumulating type incinerator and the explosion prevention main pipe is controlled to be closed; then, an electromagnetic control fireproof valve on the joint of the explosion-proof three-way pipe and the side pipe of the exhaust gas inlet pipe of the heat accumulating type incinerator is opened, an maintainer overhauls the equipment of the heat accumulating type incinerator quickly, and the organic exhaust gas to be burnt, which is burnt by the heat accumulating type incinerator, is connected into the gas inlet pipe of the gas-liquid incinerator through the side pipe of the exhaust gas inlet pipe of the heat accumulating type incinerator to continue the exhaust gas burning operation.
8. The method for using the complementary system of the gas-liquid furnace and the regenerative incinerator for waste gas treatment as claimed in claim 7, wherein: when the gas-liquid incinerator incinerates waste gas containing hydrogen, the electromagnetic control explosion-proof three-way valve is in a closed state, and the electromagnetic control fireproof valve on the three ends of the explosion-proof three-way pipe is in a closed state.
9. The method for using the complementary system of the gas-liquid furnace and the regenerative incinerator for waste gas treatment as claimed in claim 7, wherein: the air inlet pipe of the gas-liquid incinerator is communicated with a high-concentration organic waste gas source, and the air inlet pipe of the heat accumulating type incinerator is communicated with a low-concentration organic waste gas source.
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH10115411A (en) * | 1996-10-11 | 1998-05-06 | Otto:Kk | Shochu waste solution incinerator |
JPH10176819A (en) * | 1996-12-16 | 1998-06-30 | Tokyo Gas Co Ltd | Regenerative waste liquor incinerator |
CN102997247A (en) * | 2012-12-25 | 2013-03-27 | 季栋梁 | System and method for incineration treatment of saliferous waste residue, saliferous waste water and stink waste gas |
CN204254634U (en) * | 2014-11-07 | 2015-04-08 | 嘉园环保有限公司 | A kind of energy-saving organic exhaust gas incinerator |
CN108317525A (en) * | 2017-01-17 | 2018-07-24 | 恩国环保科技(上海)有限公司 | A kind of pharmaceutical technology emission-control equipment and processing method |
CN208504405U (en) * | 2018-04-13 | 2019-02-15 | 南京益农环境科技有限公司 | Incinerator in a kind of high-concentration salt-containing wastewater liquid |
KR102113585B1 (en) * | 2019-03-15 | 2020-05-22 | 주식회사 엘림글로벌 | Method for Treatment of Radioactive Organic Wastes and Apparatus for incinerating the Same |
-
2021
- 2021-09-23 CN CN202111111160.XA patent/CN113898960B/en active Active
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH10115411A (en) * | 1996-10-11 | 1998-05-06 | Otto:Kk | Shochu waste solution incinerator |
JPH10176819A (en) * | 1996-12-16 | 1998-06-30 | Tokyo Gas Co Ltd | Regenerative waste liquor incinerator |
CN102997247A (en) * | 2012-12-25 | 2013-03-27 | 季栋梁 | System and method for incineration treatment of saliferous waste residue, saliferous waste water and stink waste gas |
CN204254634U (en) * | 2014-11-07 | 2015-04-08 | 嘉园环保有限公司 | A kind of energy-saving organic exhaust gas incinerator |
CN108317525A (en) * | 2017-01-17 | 2018-07-24 | 恩国环保科技(上海)有限公司 | A kind of pharmaceutical technology emission-control equipment and processing method |
CN208504405U (en) * | 2018-04-13 | 2019-02-15 | 南京益农环境科技有限公司 | Incinerator in a kind of high-concentration salt-containing wastewater liquid |
KR102113585B1 (en) * | 2019-03-15 | 2020-05-22 | 주식회사 엘림글로벌 | Method for Treatment of Radioactive Organic Wastes and Apparatus for incinerating the Same |
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