EP3693662B1 - Inflammable waste combustion and disposal device - Google Patents
Inflammable waste combustion and disposal device Download PDFInfo
- Publication number
- EP3693662B1 EP3693662B1 EP18925057.4A EP18925057A EP3693662B1 EP 3693662 B1 EP3693662 B1 EP 3693662B1 EP 18925057 A EP18925057 A EP 18925057A EP 3693662 B1 EP3693662 B1 EP 3693662B1
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- EP
- European Patent Office
- Prior art keywords
- pressure container
- treatment device
- oxygen supply
- pressure
- crucible
- Prior art date
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- 238000002485 combustion reaction Methods 0.000 title claims description 40
- 239000002699 waste material Substances 0.000 title claims description 31
- 238000010521 absorption reaction Methods 0.000 claims description 57
- 239000007788 liquid Substances 0.000 claims description 45
- 239000000126 substance Substances 0.000 claims description 40
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 32
- 229910052760 oxygen Inorganic materials 0.000 claims description 32
- 239000001301 oxygen Substances 0.000 claims description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 32
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 25
- 229910052698 phosphorus Inorganic materials 0.000 claims description 25
- 239000011574 phosphorus Substances 0.000 claims description 25
- 239000010849 combustible waste Substances 0.000 claims description 22
- 238000001816 cooling Methods 0.000 claims description 14
- 229910052785 arsenic Inorganic materials 0.000 claims description 10
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 claims description 10
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 8
- 239000011593 sulfur Substances 0.000 claims description 8
- 229910052717 sulfur Inorganic materials 0.000 claims description 8
- 239000002253 acid Substances 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 7
- 239000003513 alkali Substances 0.000 claims description 6
- 238000005260 corrosion Methods 0.000 claims description 6
- 230000007797 corrosion Effects 0.000 claims description 6
- 239000012670 alkaline solution Substances 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 3
- 239000011241 protective layer Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 description 12
- 239000000428 dust Substances 0.000 description 7
- 239000002245 particle Substances 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 239000000779 smoke Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 208000028659 discharge Diseases 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 229910019142 PO4 Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000010452 phosphate Substances 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 2
- 239000012266 salt solution Substances 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 239000000908 ammonium hydroxide Substances 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000010811 mineral waste Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 238000004017 vitrification Methods 0.000 description 1
Images
Classifications
-
- 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
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2202/00—Combustion
- F23G2202/30—Combustion in a pressurised chamber
Definitions
- the invention relates to the technical field of environmental protection equipment, in particular to a combustible waste combustion treatment device.
- the treatment method has the following disadvantages: firstly, the phosphorus-containing substances are intensely combusted to generate a large amount of smoke and dust instantaneously, so that the activated carbon and the spraying system are difficult to completely adsorb them in a short time, and the treated offgas is difficult to reach the emission standard and pollutes the environment; secondly, the combustion tower of the treatment equipment occupies a large area and should be matched for treatment with the discharge air and offgas treatment systems, causing a high cost. There is therefore a need for more efficient treatment devices.
- US 5 606 925 A discloses a process for the incineration and vitrification of mainly mineral waste in which at least one pure or substantially pure oxygen plasma jet is used for melting the waste, the process taking place in a metal crucible containing a tapping valve and its wall is cooled by liquids flowing in internal channels.
- DE 43 28 203 A1 discloses a process which making it possible to incinerate garbage and other wastes in an odourless and smokeless manner.
- the incineration is carried out in a hermetically sealed preheated tank with a continuous supply of heated compressed air.
- the material to be incinerated is supplied in compressed form and self-ignites in the tank. This leads to a chain reaction in the tank which reduces, or renders unnecessary, a further supply of energy.
- materials having low calorific values e.g. sludge
- they can be mixed with hard coal or other combustible substances and then burnt.
- the invention provides a combustible waste combustion treatment device, which adopts the technical scheme that combustion is controlled in a closed pressure container and then the combusted products are collected into an absorption tank so as to discharge a neutral salt solution.
- the invention realizes efficient and rapid treatment of combustible wastes, and has a simple equipment structure, and it is easy to control and environment-friendly.
- a combustible waste combustion treatment device comprises a pressure container provided with a filling port, and a matched oxygen supply system, wherein a combustion system, a combusted substance absorption tank positioned on the bottom surface and an absorption liquid supply system are provided in a cavity of the pressure container; a discharge port is provided at the bottom of the combusted substance absorption tank, and a circulating water cooling system is further provided outside the cavity of the pressure container.
- the combustion system comprises a crucible positioned by means of the support frame, and a heating system by means of the periphery of the crucible, wherein an air outlet of the oxygen supply system is located above the crucible.
- the bottom of the crucible is provided with a liquid leakage hole which is in communication with the combusted substance absorption tank.
- the oxygen supply control system comprises an oxygen supply pipeline connected with an air source, an air outlet of the oxygen supply pipeline extends into the cavity of the pressure container, and the oxygen supply pipeline is provided with a pressure reducing valve and a shut-off valve.
- the device is provided with an integrated control system
- the support frame is provided with a weight sensor
- the combusted substance absorption tank is provided with a matched liquid level detector and acidity detector
- the integrated control system collects signals from the weight sensor, the liquid level detector and the acidity detector and controls corresponding valve opening for the filling port, the absorption liquid supply system and the oxygen supply system so as to realize automatic treatment.
- the device is also provided with a pressure control system comprising a safety valve and a release valve.
- a movable gate is provided at one side of the pressure container, and when the movable gate is closed, the pressure container is sealed by a snap and seal assembly.
- the pressure container is made from an acid and alkali corrosion-resistant material or the inner surface thereof is coated with an acid and alkali corrosion-resistant protective layer.
- the circulating water cooling system comprises a circulating water inlet pipe, a water cooling area provided around the cavity of the pressure container, and a circulating water return pipe which are sequentially connected with a water source at a temperature of ⁇ 40°C.
- the device is adapted to treat combustible wastes being phosphorus, phosphorus-containing wastes, arsenic, arsenic-containing wastes, sulfur and/or sulfur-containing wastes, and the combusted substance absorption tank is adapted to be filled with an alkaline solution.
- a combustible waste combustion treatment device comprising a pressure container which is a main body for treating combustible wastes, wherein the pressure container is provided with a filling port and a matched oxygen supply system;
- a circulating water cooling system is matched with the pressure container, a combustion system, a combusted substance absorption tank and an absorption liquid supply system are provided in the cavity of the pressure container, and the absorption liquid is contained in the combusted substance absorption tank and used for absorbing the combusted substances; and the circulating water cooling system is configured for removing the heat generated by the combustion reaction and reducing the temperature for the pressure container.
- the circulating water cooling system When in use, the circulating water cooling system is started, and combustible wastes enter the combustion system in the pressure container from the filling port for combustion under the cooperation of the oxygen supply system; smoke and dust particles generated by combustion are sealed in the pressure container, or subjected to gravity settling or in combination with water vapor in the cavity of the pressure container, and finally sink into the combusted substance absorption tank; a discharge port is provided at the bottom of the combusted substance absorption tank, and the smoke and dust particles can be discharged through the discharge port when the absorption effect of absorption liquid is insufficient, and the absorption liquid is then replenished by the absorption liquid supply system.
- the invention has the beneficial effects that the combustible waste combustion treatment device provided by the invention can efficiently and quickly treat combustible wastes such as waste phosphorus and phosphorus-containing wastes and realize discharge treatment with zero waste gas; the treatment speed of the wastes is controllable by the oxygen supply pressure; the device is stable in operation and easy to control in the treatment process, the substances to be treated and the alkaline solution can be added on line and the generated salt solution is discharged on line, realizing a continuous operation; the device has the advantages of small occupied area, simple structure, easiness in operation and control; and it realizes automatic control in a further improved scheme, and has low cost and a high industrial application value.
- Fig. 1 is a structurally schematic view of a combustible waste combustion treatment device according to the present invention;
- a pressure container 1-1, a filling port, 1-2, a movable gate, 2, a circulating water cooling system, 2-1, a circulating water inlet pipe, 2-2, a water cooling area, 2-3, a circulating water return pipe, 3, a crucible, 3-1, a liquid leakage hole, 3-2, a support frame, 4, a heating system, 5, an oxygen supply pipeline, 5-1, an air outlet, 5-2, a pressure reducing valve, 5-3, a shut-off valve, 6, a combusted substance absorption tank, 6-1, a discharge port, 6-2, an absorption liquid supply system, 7, a safety valve, 8 and a release valve.
- the treatment device includes a pressure container 1, wherein the pressure container is provided with a filling port 1-1 and a matched oxygen supply system; the oxygen supply system includes an oxygen supply pipeline 5 connected with an oxygen source, the oxygen supply pipeline 5 is provided with a pressure reducing valve 5-2 and a shut-off valve 5-3, and the pressure reducing valve 5-2 is configured for controlling and stabilizing the oxygen pressure in the pressure container 1, so that the combustion rate is controlled; and an air outlet 5-1 of the oxygen supply pipeline 5 extends into the cavity of the pressure container 1.
- a combustion system is provided in the cavity of the pressure container 1, and the combustion system includes a crucible 3 positioned by means of a support frame 3-2 and a heating system 4 provided at the periphery of the crucible 3; an air outlet 5-1 of an oxygen supply pipeline 5 is located above the crucible 3; and the heating system 4 is configured for heating the crucible 3, so that combustible wastes in the crucible 3 can reach an ignition point, and the combustion state is maintained under the combustion supporting of oxygen.
- a combusted substance absorption tank 6 is provided below the crucible 3, absorption liquid is contained in the combusted substance absorption tank and used for absorbing combusted substances, and a discharge port 6-1 is provided at the bottom of the combusted substance absorption tank 6; when the absorption liquid absorbs the combusted substances until the effectiveness thereof is insufficient, the absorption liquid can be discharged through the discharge port 6-1, and an absorption liquid supply system is matched with the combusted substance absorption tank 6 and configured for replenishing the absorption liquid.
- a circulating water cooling system is provided outside the cavity of the pressure container 1 and includes a circulating water inlet pipe 2-1, a water cooling area 2-2 provided around the cavity of the pressure container 1, and a circulating water return pipe 2-3 which are sequentially connected with a water source at a temperature of ⁇ 40°C.
- the bottom of the crucible 3 is provided with a liquid leakage hole 3-1 which is in communication with the combusted substance absorption tank 6.
- the device is further provided with a pressure control system including a safety valve 7 and a release valve 8.
- a movable gate 1-2 is provided at one side of the pressure container 1, and when the movable gate 1-2 is closed, the pressure container 1 is sealed by a snap and seal assembly, so that substances such as particles generated after combustion will not overflow to the environment to generate pollution, danger and the like; besides, due to the arrangement of the movable gate 1-2, it facilitates the operation of cleaning the crucible 3 and the like.
- a compression-resistant material and a thickness are selected for the pressure container 1 according to the treatment capacity and the material performance parameters; and in order to ensure the use safety and the service life of the treatment device, the pressure container 1 is made of an acid and alkali resistant and corrosion-resistant material or the inner surface thereof is coated with a protective layer with acid and alkali resistant and corrosion-resistant properties.
- the treatment device is mainly used for treating combustible wastes such as phosphorus, phosphorus-containing wastes, arsenic, arsenic-containing wastes, arsenic, arsenic-containing wastes, sulfur and/or sulfur-containing wastes and the like, the combusted substances formed after the wastes are combusted settle into the combusted substance absorption tank, or the combusted substances and the water vapor in the pressure container 1 are combined to form liquid drops and settle into the combusted substance absorption tank so as to realize harmless collection treatment.
- the application method of the treatment device is illustrated by taking waste phosphorus and phosphorus-containing wastes as examples.
- the pressure maintaining process in the treatment process is as follows: oxygen consumed by combustion is continuously supplied by an oxygen supply system under the accurate control of the pressure reducing valve so as to ensure the continuous combustion; besides, since the pressure container 1 stays in a normal pressure state before being closed, nitrogen in the air is always in the container, and no nitrogen is consumed in the combustion process, so that the atmosphere in the pressure container 1 is safe;
- the adding process of waste adding and alkaline absorption liquid on line in the process of batch treatment of phosphorus-containing wastes includes the following steps: the pressure of the pressure reducing valve 5-2 is to 0.1 MPa; after the pressure in the pressure container 1 is stable, the release valve 8 is opened; then the plate valve on the filling port 1-1 is opened, wastes are added to the crucible 3 through the filling port 1-1, and then the plate valve is closed, so that the wastes to be treated are added on line; meanwhile, the absorption liquid can be added on line by opening a valve of the absorption liquid supply system 6-2;
- an integrated control system is provided in the combustible waste combustion treatment device of the example, a weight sensor is provided on the support frame 3-2 of the crucible 3 to weigh the wastes to be treated in the crucible 3; a matched liquid level detector and an acidity detector are provided in the combusted substance absorption tank 6, and a signal acquisition end of the integrated control system is respectively connected with the weight sensor, the liquid level detector and the acidity detector; a signal output end thereof is respectively connected with a plate valve on the filling port 1-1 and a valve on the absorption liquid supply system 6-2; when the weight of the crucible 3 is lower than a set low limit value, the integrated control system controls the plate valve on the filling port 1-1 to open the filling to a set range or a high limit value; when the liquid level detector detects that the liquid level is too low or the acidity detector detects that the pH value is greater than a set value, the integrated control system controls to open a valve on the absorption liquid supply system 6-2 for replenish
- the treatment device is further provided with a pressure sensor for detecting the pressure in the cavity, a signal acquisition end of the integrated control system is connected with the pressure sensor, and a signal output end thereof is respectively connected with a shut-off valve 5-3 and a pressure reducing valve 5-2 on an oxygen supply pipeline 5, so that the pressure container 1 is controlled under a constant pressure.
- the characteristics that phosphorus, arsenic, sulfur and the like are easy to combust and products dissolve in water easily are utilized, so that the waste phosphorus, the phosphorus-containing wastes and the like are subjected to combustion reaction with oxygen at a constant pressure and proportion in the pressure container 1, and the products are further settled and absorbed until being safely and harmlessly discharged, realizing the high-efficiency and zero-waste gas and dust treatment, and greatly improving the safety. It realizes the automatic control treatment, and can be applied for industrial application easily.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Treating Waste Gases (AREA)
- Processing Of Solid Wastes (AREA)
- Gasification And Melting Of Waste (AREA)
Description
- The invention relates to the technical field of environmental protection equipment, in particular to a combustible waste combustion treatment device.
- In industrial production, it is inevitable to produce lots of combustible wastes, such as phosphorus, arsenic, sulfur, carbon and so on. The generation of combustible wastes has a great threat to safe production in some production lines, and its treatment is a difficult matter. In the production of semiconductors, the treatment of phosphorus and phosphorus-containing wastes has always been a difficulty. Now the phosphorus and phosphorus-containing wastes are put in a combustion tower for combustion treatment in the main treatment method. Due to the generation of a large amount of smoke and dust particles in a short time in the combustion process, the adsorption and dust removal treatment is generally followed after the combustion, and the smoke and dust particles are passed through an activated carbon or spray type offgas treatment system. At present, the treatment method has the following disadvantages: firstly, the phosphorus-containing substances are intensely combusted to generate a large amount of smoke and dust instantaneously, so that the activated carbon and the spraying system are difficult to completely adsorb them in a short time, and the treated offgas is difficult to reach the emission standard and pollutes the environment; secondly, the combustion tower of the treatment equipment occupies a large area and should be matched for treatment with the discharge air and offgas treatment systems, causing a high cost. There is therefore a need for more efficient treatment devices.
-
US 5 606 925 A discloses a process for the incineration and vitrification of mainly mineral waste in which at least one pure or substantially pure oxygen plasma jet is used for melting the waste, the process taking place in a metal crucible containing a tapping valve and its wall is cooled by liquids flowing in internal channels. -
DE 43 28 203 A1 discloses a process which making it possible to incinerate garbage and other wastes in an odourless and smokeless manner. The incineration is carried out in a hermetically sealed preheated tank with a continuous supply of heated compressed air. The material to be incinerated is supplied in compressed form and self-ignites in the tank. This leads to a chain reaction in the tank which reduces, or renders unnecessary, a further supply of energy. For the self-ignition and the incineration of materials having low calorific values, e.g. sludge, they can be mixed with hard coal or other combustible substances and then burnt. - In order to solve the technical problems that the existing combustible waste treatment equipment has high cost, large occupied space and heavy offgas pollution, the invention provides a combustible waste combustion treatment device, which adopts the technical scheme that combustion is controlled in a closed pressure container and then the combusted products are collected into an absorption tank so as to discharge a neutral salt solution. The invention realizes efficient and rapid treatment of combustible wastes, and has a simple equipment structure, and it is easy to control and environment-friendly.
- According to the technical scheme adopted by the invention, a combustible waste combustion treatment device comprises a pressure container provided with a filling port, and a matched oxygen supply system, wherein a combustion system, a combusted substance absorption tank positioned on the bottom surface and an absorption liquid supply system are provided in a cavity of the pressure container; a discharge port is provided at the bottom of the combusted substance absorption tank, and a circulating water cooling system is further provided outside the cavity of the pressure container.
- Further, the combustion system comprises a crucible positioned by means of the support frame, and a heating system by means of the periphery of the crucible, wherein an air outlet of the oxygen supply system is located above the crucible.
- Further, the bottom of the crucible is provided with a liquid leakage hole which is in communication with the combusted substance absorption tank.
- Further, the oxygen supply control system comprises an oxygen supply pipeline connected with an air source, an air outlet of the oxygen supply pipeline extends into the cavity of the pressure container, and the oxygen supply pipeline is provided with a pressure reducing valve and a shut-off valve.
- Further, the device is provided with an integrated control system, the support frame is provided with a weight sensor, the combusted substance absorption tank is provided with a matched liquid level detector and acidity detector, the integrated control system collects signals from the weight sensor, the liquid level detector and the acidity detector and controls corresponding valve opening for the filling port, the absorption liquid supply system and the oxygen supply system so as to realize automatic treatment.
- Further, the device is also provided with a pressure control system comprising a safety valve and a release valve.
- Further, a movable gate is provided at one side of the pressure container, and when the movable gate is closed, the pressure container is sealed by a snap and seal assembly.
- Further, the pressure container is made from an acid and alkali corrosion-resistant material or the inner surface thereof is coated with an acid and alkali corrosion-resistant protective layer.
- Further, the circulating water cooling system comprises a circulating water inlet pipe, a water cooling area provided around the cavity of the pressure container, and a circulating water return pipe which are sequentially connected with a water source at a temperature of ≤ 40°C.
- Further, the device is adapted to treat combustible wastes being phosphorus, phosphorus-containing wastes, arsenic, arsenic-containing wastes, sulfur and/or sulfur-containing wastes, and the combusted substance absorption tank is adapted to be filled with an alkaline solution.
- According to the above technical scheme, it provides a combustible waste combustion treatment device comprising a pressure container which is a main body for treating combustible wastes, wherein the pressure container is provided with a filling port and a matched oxygen supply system; as a key design of the invention, a circulating water cooling system is matched with the pressure container, a combustion system, a combusted substance absorption tank and an absorption liquid supply system are provided in the cavity of the pressure container, and the absorption liquid is contained in the combusted substance absorption tank and used for absorbing the combusted substances; and the circulating water cooling system is configured for removing the heat generated by the combustion reaction and reducing the temperature for the pressure container. When in use, the circulating water cooling system is started, and combustible wastes enter the combustion system in the pressure container from the filling port for combustion under the cooperation of the oxygen supply system; smoke and dust particles generated by combustion are sealed in the pressure container, or subjected to gravity settling or in combination with water vapor in the cavity of the pressure container, and finally sink into the combusted substance absorption tank; a discharge port is provided at the bottom of the combusted substance absorption tank, and the smoke and dust particles can be discharged through the discharge port when the absorption effect of absorption liquid is insufficient, and the absorption liquid is then replenished by the absorption liquid supply system.
- The invention has the beneficial effects that the combustible waste combustion treatment device provided by the invention can efficiently and quickly treat combustible wastes such as waste phosphorus and phosphorus-containing wastes and realize discharge treatment with zero waste gas; the treatment speed of the wastes is controllable by the oxygen supply pressure; the device is stable in operation and easy to control in the treatment process, the substances to be treated and the alkaline solution can be added on line and the generated salt solution is discharged on line, realizing a continuous operation; the device has the advantages of small occupied area, simple structure, easiness in operation and control; and it realizes automatic control in a further improved scheme, and has low cost and a high industrial application value.
-
Fig. 1 is a structurally schematic view of a combustible waste combustion treatment device according to the present invention;
In thefigure: 1 , a pressure container, 1-1, a filling port, 1-2, a movable gate, 2, a circulating water cooling system, 2-1, a circulating water inlet pipe, 2-2, a water cooling area, 2-3, a circulating water return pipe, 3, a crucible, 3-1, a liquid leakage hole, 3-2, a support frame, 4, a heating system, 5, an oxygen supply pipeline, 5-1, an air outlet, 5-2, a pressure reducing valve, 5-3, a shut-off valve, 6, a combusted substance absorption tank, 6-1, a discharge port, 6-2, an absorption liquid supply system, 7, a safety valve, 8 and a release valve. - Hereinafter, the structure and use method of a combustible waste combustion treatment device provided by the present invention will be described in detail with specific examples.
- The example provides a combustible waste combustion treatment device; as shown in
Fig. 1 , the treatment device includes apressure container 1, wherein the pressure container is provided with a filling port 1-1 and a matched oxygen supply system; the oxygen supply system includes anoxygen supply pipeline 5 connected with an oxygen source, theoxygen supply pipeline 5 is provided with a pressure reducing valve 5-2 and a shut-off valve 5-3, and the pressure reducing valve 5-2 is configured for controlling and stabilizing the oxygen pressure in thepressure container 1, so that the combustion rate is controlled; and an air outlet 5-1 of theoxygen supply pipeline 5 extends into the cavity of thepressure container 1. A combustion system is provided in the cavity of thepressure container 1, and the combustion system includes acrucible 3 positioned by means of a support frame 3-2 and a heating system 4 provided at the periphery of thecrucible 3; an air outlet 5-1 of anoxygen supply pipeline 5 is located above thecrucible 3; and the heating system 4 is configured for heating thecrucible 3, so that combustible wastes in thecrucible 3 can reach an ignition point, and the combustion state is maintained under the combustion supporting of oxygen. A combustedsubstance absorption tank 6 is provided below thecrucible 3, absorption liquid is contained in the combusted substance absorption tank and used for absorbing combusted substances, and a discharge port 6-1 is provided at the bottom of the combustedsubstance absorption tank 6; when the absorption liquid absorbs the combusted substances until the effectiveness thereof is insufficient, the absorption liquid can be discharged through the discharge port 6-1, and an absorption liquid supply system is matched with the combustedsubstance absorption tank 6 and configured for replenishing the absorption liquid. In order to reduce the excessive heat generated by the combustion reaction in thepressure container 1 and decrease the temperature of thepressure container 1, a circulating water cooling system is provided outside the cavity of thepressure container 1 and includes a circulating water inlet pipe 2-1, a water cooling area 2-2 provided around the cavity of thepressure container 1, and a circulating water return pipe 2-3 which are sequentially connected with a water source at a temperature of ≤ 40°C. - In order to avoid that the combusted substances or the liquid drops formed by the combusted substances combined with the water vapor in the cavity of the
pressure container 1 settle into thecrucible 3 to cover the wastes to be combusted, so that the treatment is interrupted, the bottom of thecrucible 3 is provided with a liquid leakage hole 3-1 which is in communication with the combustedsubstance absorption tank 6. - In order to prevent danger caused by accidental excessive pressure in the
pressure container 1, the device is further provided with a pressure control system including asafety valve 7 and arelease valve 8. - A movable gate 1-2 is provided at one side of the
pressure container 1, and when the movable gate 1-2 is closed, thepressure container 1 is sealed by a snap and seal assembly, so that substances such as particles generated after combustion will not overflow to the environment to generate pollution, danger and the like; besides, due to the arrangement of the movable gate 1-2, it facilitates the operation of cleaning thecrucible 3 and the like. - A compression-resistant material and a thickness are selected for the
pressure container 1 according to the treatment capacity and the material performance parameters; and in order to ensure the use safety and the service life of the treatment device, thepressure container 1 is made of an acid and alkali resistant and corrosion-resistant material or the inner surface thereof is coated with a protective layer with acid and alkali resistant and corrosion-resistant properties. - The treatment device is mainly used for treating combustible wastes such as phosphorus, phosphorus-containing wastes, arsenic, arsenic-containing wastes, arsenic, arsenic-containing wastes, sulfur and/or sulfur-containing wastes and the like, the combusted substances formed after the wastes are combusted settle into the combusted substance absorption tank, or the combusted substances and the water vapor in the
pressure container 1 are combined to form liquid drops and settle into the combusted substance absorption tank so as to realize harmless collection treatment. The application method of the treatment device is illustrated by taking waste phosphorus and phosphorus-containing wastes as examples. - (1) Filling: opening a movable gate 1-2 of a
pressure container 1 under a common atmospheric pressure environment, opening a plate valve on a filling port 17, pouring phosphorus-containing wastes for combustion treatment into acrucible 3 from the filling port 17, and closing the plate valve after the filling is completed; - (2) Liquid adding: opening a valve on an absorption liquid supply system 6-2, injecting an alkaline solution such as ammonium hydroxide and limewater into the combusted
substance absorption tank 6, and stopping injection after reaching a specified liquid level; - (3) Pressurizing: closing the movable gate 1-2, opening a shut-off valve 5-3 on an
oxygen supply pipeline 5, adjusting the pressure reducing valve 5-2 to the required pressure, generally requiring 0.1-0.5MPa, and controlling the pressure to 0.1 MPa in the example; - (4) Circulating water: opening a circulating water cooling system;
- (5) Combusting: starting a heating system 4, and burning the phosphorus when the temperature in the
crucible 3 reaches the ignition point of the phosphorus; - (6) Adsorbing and settling: the product from phosphorus combustion is diffused in the
pressure container 1, but no emission exists; part of the combusted substance particles settle to the combustedsubstance absorption tank 6 under the action of gravity; and in addition, due to the fact that the temperature in thepressure container 1 is high and the water vapor pressure is high, part of the combusted substances can be combined with the water vapor to form acid liquid drops and then also settle to the combustedsubstance absorption tank 6 for acid-base neutralization with the absorption liquid in the combustedsubstance absorption tank 6 to form phosphate; - (7) Discharging: when the phosphorus-containing wastes to be treated are treated completely or the absorption effect of the absorption liquid is insufficient, the pressure of the pressure reducing valve 5-2 is adjusted to 0.1 MPa; after the pressure in the
pressure container 1 is stabilized, the discharge port 6-1 is opened to discharge the phosphate solution, the absorption liquid is replenished by the absorption liquid replenishing system 6-2, and the treatment is finished. - The pressure maintaining process in the treatment process is as follows: oxygen consumed by combustion is continuously supplied by an oxygen supply system under the accurate control of the pressure reducing valve so as to ensure the continuous combustion; besides, since the
pressure container 1 stays in a normal pressure state before being closed, nitrogen in the air is always in the container, and no nitrogen is consumed in the combustion process, so that the atmosphere in thepressure container 1 is safe;
The adding process of waste adding and alkaline absorption liquid on line in the process of batch treatment of phosphorus-containing wastes includes the following steps: the pressure of the pressure reducing valve 5-2 is to 0.1 MPa; after the pressure in thepressure container 1 is stable, therelease valve 8 is opened; then the plate valve on the filling port 1-1 is opened, wastes are added to thecrucible 3 through the filling port 1-1, and then the plate valve is closed, so that the wastes to be treated are added on line; meanwhile, the absorption liquid can be added on line by opening a valve of the absorption liquid supply system 6-2; - On the basis of the example 1, an integrated control system is provided in the combustible waste combustion treatment device of the example, a weight sensor is provided on the support frame 3-2 of the
crucible 3 to weigh the wastes to be treated in thecrucible 3; a matched liquid level detector and an acidity detector are provided in the combustedsubstance absorption tank 6, and a signal acquisition end of the integrated control system is respectively connected with the weight sensor, the liquid level detector and the acidity detector; a signal output end thereof is respectively connected with a plate valve on the filling port 1-1 and a valve on the absorption liquid supply system 6-2; when the weight of thecrucible 3 is lower than a set low limit value, the integrated control system controls the plate valve on the filling port 1-1 to open the filling to a set range or a high limit value; when the liquid level detector detects that the liquid level is too low or the acidity detector detects that the pH value is greater than a set value, the integrated control system controls to open a valve on the absorption liquid supply system 6-2 for replenishing the absorption liquid to a high liquid level so as to ensure higher absorption efficiency. - The treatment device is further provided with a pressure sensor for detecting the pressure in the cavity, a signal acquisition end of the integrated control system is connected with the pressure sensor, and a signal output end thereof is respectively connected with a shut-off valve 5-3 and a pressure reducing valve 5-2 on an
oxygen supply pipeline 5, so that thepressure container 1 is controlled under a constant pressure. - According to the combustible waste combustion treatment device, the characteristics that phosphorus, arsenic, sulfur and the like are easy to combust and products dissolve in water easily are utilized, so that the waste phosphorus, the phosphorus-containing wastes and the like are subjected to combustion reaction with oxygen at a constant pressure and proportion in the
pressure container 1, and the products are further settled and absorbed until being safely and harmlessly discharged, realizing the high-efficiency and zero-waste gas and dust treatment, and greatly improving the safety. It realizes the automatic control treatment, and can be applied for industrial application easily.
Claims (10)
- A combustible waste combustion treatment device comprising a pressure container (1) provided with a filling port (1-1) and a matched oxygen supply system, characterized in that a combustion system, a combusted substance absorption tank (6) positioned on the bottom surface and an absorption liquid supply system (6-2) are provided in a cavity of the pressure container (1); a discharge port (6-1) is provided at the bottom of the combusted substance absorption tank (6), and a circulating water cooling system is further provided outside the cavity of the pressure container (1).
- The treatment device according to claim 1, characterized in that the combustion system comprises a crucible (3) positioned by means of a support frame (3-2), and a heating system (4) provided at the periphery of the crucible (3), wherein an air outlet (5-1) of the oxygen supply system is located above the crucible (3).
- The treatment device according to claim 2, characterized in that the bottom of the crucible (3) is provided with a liquid leakage hole (3-1) which is in communication with the combusted substance absorption tank (6).
- The treatment device according to claim 3, characterized in that the device is provided with an integrated control system, the support frame (3-2) is provided with a weight sensor, the combusted substance absorption tank (6) is provided with a matched liquid level detector and acidity detector, the integrated control system collects signals from the weight sensor, the liquid level detector and the acidity detector and controls corresponding valve opening for the filling port (1-1), the absorption liquid supply system (6-2) and the oxygen supply system so as to realize automatic treatment.
- The treatment device according to claim 1, characterized in that the oxygen supply control system comprises an oxygen supply pipeline (5) connected with an air source, an air outlet (5-1) of the oxygen supply pipeline (5) extends into the cavity of the pressure container (1), and the oxygen supply pipeline (5) is provided with a pressure reducing valve (5-2) and a shut-off valve (5-3).
- The treatment device according to claim 1, characterized in that the device is further provided with a pressure control system comprising a safety valve (7) and a release valve (8).
- The treatment device according to claim 1, characterized in that a movable gate (1-2) is provided at one side of the pressure container (1), and when the movable gate (1-2) is closed, the pressure container (1) is sealed by a snap and seal assembly.
- The treatment device according to claim 1 or 7, characterized in that the pressure container (1) is made from an acid and alkali corrosion-resistant material or the inner surface thereof is coated with an acid and alkali corrosion-resistant protective layer.
- The treatment device according to claim 1, characterized in that the circulating water cooling system comprises a circulating water inlet pipe (2-1), a water cooling area (2-2) provided around the cavity of the pressure container (1), and a circulating water return pipe (2-3) which are sequentially connected with a water source at a temperature of ≤ 40°C.
- The treatment device according to claim 1, characterized in that the device is adapted to treat combustible wastes being phosphorus, phosphorus-containing wastes, arsenic, arsenic-containing wastes, sulfur and/or sulfur-containing wastes, and the combusted substance absorption tank is adapted to be filled with an alkaline solution.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811521947.1A CN109373333B (en) | 2018-12-13 | 2018-12-13 | Inflammable waste combustion treatment device |
PCT/CN2018/122629 WO2020118756A1 (en) | 2018-12-13 | 2018-12-21 | Inflammable waste combustion and disposal device |
Publications (3)
Publication Number | Publication Date |
---|---|
EP3693662A1 EP3693662A1 (en) | 2020-08-12 |
EP3693662A4 EP3693662A4 (en) | 2020-11-25 |
EP3693662B1 true EP3693662B1 (en) | 2021-08-04 |
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ID=65374310
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Application Number | Title | Priority Date | Filing Date |
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EP18925057.4A Active EP3693662B1 (en) | 2018-12-13 | 2018-12-21 | Inflammable waste combustion and disposal device |
Country Status (3)
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EP (1) | EP3693662B1 (en) |
CN (1) | CN109373333B (en) |
WO (1) | WO2020118756A1 (en) |
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CN112705016B (en) * | 2020-12-30 | 2022-11-25 | 四川雅吉芯电子科技有限公司 | Waste gas treatment system is used in production of monocrystalline silicon epitaxial wafer |
CN114544855B (en) * | 2022-02-08 | 2024-02-02 | 内蒙古众元测试技术有限公司 | Detection device for nonmetallic element content in waste |
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JPH0712717U (en) * | 1993-07-23 | 1995-03-03 | 昌美 氷室 | Smokeless / closed room incinerator |
DE4328203A1 (en) * | 1993-08-21 | 1995-03-16 | Jonathan Bohn | Process for incinerating refuse, toxic substances and wastes in a hermetic tank |
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JPH10185135A (en) * | 1996-12-24 | 1998-07-14 | Shigeo Matsuura | Incineration treatment of nonflammable plastic waste generating hydrogen chloride and dioxin group and incinerator |
KR200178489Y1 (en) * | 1999-10-11 | 2000-04-15 | 동국산업주식회사 | Sludge incineration facility |
JP2001242291A (en) * | 2000-02-25 | 2001-09-07 | Ngk Insulators Ltd | Device and method for incineration melting disposal of radioactive waste |
JP3838617B2 (en) * | 2000-03-27 | 2006-10-25 | 日本碍子株式会社 | Waste incineration method |
CN2861769Y (en) * | 2005-10-12 | 2007-01-24 | 吴桐 | Hydrogen/oil mixed waste incinerator |
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CN201764539U (en) * | 2010-06-23 | 2011-03-16 | 中北大学 | Novel environment-friendly energy-saving coal stove |
CN102168852A (en) * | 2010-12-23 | 2011-08-31 | 北京机电院高技术股份有限公司 | Method and device for reducing emission limits of nitrogen oxides in waste incineration flue gas |
CN102226517B (en) * | 2011-04-26 | 2013-09-18 | 于政钦 | Heat facility burning device with pyrolysis gasification and low oxygen combustion functions |
KR20130055390A (en) * | 2011-11-18 | 2013-05-28 | 최영석 | After-incineration reprocessing method for radioactive waste and the same apparatus |
CN203687059U (en) * | 2013-12-16 | 2014-07-02 | 六九硅业有限公司 | Burning device for treating production tail gas of polycrystalline silicon |
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CN205965423U (en) * | 2016-08-22 | 2017-02-22 | 深圳市华保科技有限公司 | Burning absorbing device |
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2018
- 2018-12-13 CN CN201811521947.1A patent/CN109373333B/en active Active
- 2018-12-21 EP EP18925057.4A patent/EP3693662B1/en active Active
- 2018-12-21 WO PCT/CN2018/122629 patent/WO2020118756A1/en unknown
Also Published As
Publication number | Publication date |
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CN109373333B (en) | 2024-08-13 |
WO2020118756A1 (en) | 2020-06-18 |
CN109373333A (en) | 2019-02-22 |
EP3693662A1 (en) | 2020-08-12 |
EP3693662A4 (en) | 2020-11-25 |
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