CN108332214B - A kind of medical waste substance treating method - Google Patents
A kind of medical waste substance treating method Download PDFInfo
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- CN108332214B CN108332214B CN201810152803.7A CN201810152803A CN108332214B CN 108332214 B CN108332214 B CN 108332214B CN 201810152803 A CN201810152803 A CN 201810152803A CN 108332214 B CN108332214 B CN 108332214B
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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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/54—Nitrogen compounds
- B01D53/56—Nitrogen oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/60—Simultaneously removing sulfur oxides and nitrogen oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/76—Gas phase processes, e.g. by using aerosols
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/81—Solid phase processes
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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
- F23G5/44—Details; Accessories
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/003—Arrangements of devices for treating smoke or fumes for supplying chemicals to fumes, e.g. using injection devices
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/40—Alkaline earth metal or magnesium compounds
- B01D2251/404—Alkaline earth metal or magnesium compounds of calcium
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/60—Inorganic bases or salts
- B01D2251/602—Oxides
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
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Abstract
The present invention relates to a kind of medical waste substance treating method, the processing method uses medical waste treatment device, and the medical waste treatment device includes incinerator, mixing tube, primary adsorption room, secondary absorption room, critical reaction chamber and disengagement chamber.By the specific medical waste substance treating method of setting collocation of specific device, so that the processing method of existing known critical water process medical treatment flying ash can be realized flue gas and water and all re-start processing and reach complete harmless treatment.To not cause secondary pollution to atmosphere and water during handling Biohazard Waste.
Description
Technical field
The invention belongs to medical fields and field of waste recycle, and in particular to a kind of medical waste substance treating method.
Background technique
Since the comparison of ingredients of Biohazard Waste is complicated, in order to avoid the secondary propagation of the harmful organisms such as bacterial virus, mesh
It is preceding mainly the mode of burning to be taken to be handled, but since Biohazard Waste is other than harmful microorganism, it is also possible to contain
A large amount of heavy metal element and other harmful elements, flue gas and burning ash after burning can make environment if direct emission
At secondary pollution.Supercritical water treatment flying ash becomes handles a kind of relatively effective method of medical flying ash at present, but
It is the liquid for having dissolved a large amount of harmful substances to be taken into conventional plus alkali separation method, low separation efficiency at present, and separate effect
Fruit is not very good.And incineration flue gas is mainly discharged by the way of direct emission at present.To in processing solid waste
Gas and liquid debris are produced when object again, so that the processing mode environmental friendliness is bad.
Summary of the invention
Of the invention proposes a kind of medical waste substance treating method.
It is realized by following technological means:
A kind of medical waste substance treating method, the processing method use medical waste treatment device, and the medical treatment is useless
Gurry processing unit includes incinerator, mixing tube, primary adsorption room, secondary absorption room, critical reaction chamber and disengagement chamber.
The incinerator includes burning stove outer covering, incinerator outlet flue and incinerator ash hole, the burning stove outer covering to be in
Upper hollow cylindrical body lower hopper shape structure setting, is provided with porous plate, the porous plate is used between the upper
The burning ash that top incinerated matter generates is drained into lower part, the incinerator cover top portion is provided with incinerator outlet flue, at it
Lower hopper shape structure bottom end forms incinerator ash hole.
The mixing tube includes shell, carbonated drink spray head, ozone spray head and contraction mouth, and the shell is that vertical tubular structure is set
It sets, shell top is provided with the contraction mouth of upside down funnel shape, the shell lower part is connected with the incinerator outlet flue, institute
It states shell and tube sides portion and is respectively arranged with carbonated drink spray head and ozone spray head, it is mixed to be respectively used to the inside of mixing tube to spray carbonated drink obliquely
Close object and ozone.
The primary adsorption room includes level-one chamber enclosure, level-one chamber inlet, the outlet of level-one room and calcium oxide particle and work
Property charcoal particle；The calcium oxide particle and active carbon particle, which uniformly gather, to be distributed in the level-one chamber enclosure, outside level-one room
Shell bottom side is provided with level-one chamber inlet, and shell-side top is provided with the outlet of level-one room outside level-one room；The level-one room enters
Mouth is connected with the contraction mouth top.
The secondary absorption room includes second level chamber enclosure, secondary absorption chamber inlet, processing exhanst gas outlet and oxidation calcisphere；Institute
It states secondary absorption chamber inlet to be arranged in secondary chamber outer casing bottom, and is connected with level-one room outlet, the processing flue gas
Outlet is arranged in secondary chamber cover top portion side, and the oxidation calcisphere is uniformly distributed in the second level chamber enclosure.
The critical reaction chamber include reaction chamber enclosure, pure water, heating rod, gas siphunculus, air pump, pure water siphunculus,
Water pump, reaction chamber entrance and reaction chamber outlet；Reaction chamber entrance setting reaction chamber cover top portion and with the incinerator
Ash hole is connected, and is recessed downwards in the reaction chamber outer casing bottom and forms the reaction chamber outlet, in the reaction chamber enclosure
Interior bottom is vertically arranged with multiple heating rods, and reaction chamber top side wall is provided with gas siphunculus, sets on the gas siphunculus
It is equipped with air pump, the gas siphunculus and air pump are used to adjust critical reaction chamber internal pressure by the injection and extraction of gas,
Reaction chamber side wall middle and upper part is provided with pure water siphunculus and water pump, the pure water siphunculus and water pump are used for reaction chamber enclosure
Inside injection pure water, the pure water is set to reaction chamber interior of shell, and the height of pure water is that reaction chamber enclosure is high
The 50% ~ 68% of degree.
The disengagement chamber includes filter plate, outer filter plate inner membrance, the outer filter plate of arc, support in separation chamber enclosure, arc
Axis, disengagement chamber entrance and processing water out；The separation chamber enclosure is hollow rectangular parallelepiped structure, is provided with point in its center of top
From chamber entrance, the disengagement chamber entrance is connected with reaction chamber outlet, sets gradually immediately below the disengagement chamber entrance
There is the outer filter plate of filter plate in the arc of the hollow hemisphere bodily form, outer filter plate inner membrance and arc, the outer filter plate inner membrance is close to
In inside filter plate, filter plate bottom is vertically arranged with support outside filter plate in the arc and arc outside the arc
Axis, filter plate and the outer filter plate of arc are densely covered porous plate in the arc, the support shaft bottom by bearing with it is described
The rotation of disengagement chamber outer casing bottom is affixed, and filter plate and the outer filter plate of arc can be rotated by axis of support shaft in the arc, institute
Support shaft is stated as hollow structure setting, the hollow structure is being provided with out between filter plate outside filter plate in arc and arc
Mouthful, for by alkaline matter by being placed to inside support shaft in arc outside filter plate and arc between filter plate；At described point
Chamber enclosure side bottom is provided with processing water out.
The medical waste substance treating method includes the following steps.
(1) Biohazard Waste is placed in incinerator and is burned, the flue gas for burning generation passes through incinerator outlet flue
It enters in mixing tube, the burning ash for burning generation is entered in critical reaction chamber by incinerator ash hole.
(2) flue gas for burning generation, which enters in mixing tube, moves upwards, and starts carbonated drink spray head and ozone spray head, to
Steam water interface and ozone are sprayed in flue gas, so that flue gas brings moisture into uphill process, while ozone is to therein low
Valence nitrogen oxides are the nitrogen oxides of high price, and the water adsorption dissolution being injected into.
(3) flue gas improves gas pressure by contraction mouth and accelerates into primary adsorption room, aqueous sulphur in flue gas
Oxide and the aqueous nitrogen oxides being oxidized are reacted with calcium oxide particle, while the heavy metal element in flue gas is oxidized calcium
Particle and active carbon particle absorption.
(4) flue gas enters in secondary absorption room from primary adsorption room, and the calcium oxide particle in secondary absorption room is by flue gas
The water adsorption of middle remnants, then by processing exhanst gas outlet will treated flue gas emission into air.
(5) burning ash is entered in critical reaction chamber by incinerator ash hole, and critical reaction is intracavitary to be provided with pure water,
Start and the intracavitary pressure of critical reaction is adjusted by gas pipeline and air pump while heating rod heats pure water, so that critical
Pressure and temperature in reaction chamber reaches the critical pressure and critical-temperature of supercritical water so that pure water by burning ash a huge sum of money
Belong to element dissolution.
(6) reaction chamber outlet is opened, solidliquid mixture is discharged into disengagement chamber, while opening motor and making mistake in arc
Filter plate and the outer filter plate of arc are around support shaft high speed rotation, so that solid ash content is maintained at liquid separation in filter plate in arc
In to arc outside filter plate and arc between filter plate, the opening being then turned in support shaft releases alkaline matter, continues high
After a certain period of time, outer filter plate inner membrance is extracted away for speed rotation, continues high speed rotation, thus the heavy metal that will be obtained after reaction
Alkaloid substance is maintained in the outer filter plate of arc, and the processing water after handling is split into the disengagement chamber outside the outer filter plate of arc
In shell, then pass through processing water out discharge.
Preferably, the intracavitary pressure of the critical reaction is 22.1MPa, the temperature of pure water is 374 DEG C and (forms super faces
The pressure and temperature of boundary's water).
Preferably, continuation high speed rotation certain time described in step (6) is specially 3 ~ 5min.
Preferably, opening support shaft top after filter plate rotation outside filter plate in arc and arc in step (6)
Portion's opening solid ash content is discharged downwards by support shaft, then by opening support shaft side mouth for filter plate outside arc
Interior heavy metal alkaloid substance passes through discharge downwards inside support shaft.
Preferably, alkaline matter described in step (6) is calcium hydroxide.
Preferably, the support shaft is detachable.
Effect of the invention is that:
1, both the flue gas for burning generation was handled, while having carried out the nocuousness such as heavy metal to the flying dust generated is burned
Substance processing, and the water to contain hazardous substance after processing has also carried out separating-adding alkali reaction-separation mode to processing water
It is handled, to realize the full processing of solid, liquid, gas, is truly realized harmless treatment.
2, it burns in the flue gas of generation containing lower nitrogen oxides and oxysulfide, by spraying ozone, while also spraying
Steam water interface, so that lower nitrogen oxides are relatively high higher nitrogen oxides, then higher nitrogen oxides by ozone
Be dissolved in water (trivalent and pentavalent nitrogen oxides is only absorbed by the water to form acid), at the same oxysulfide be also dissolved in water it is (anti-with water
Acid should be formed), flue gas enters in primary adsorption room with these acid solutions, and steam dissolves calcium oxide particle surface to form hydrogen
Calcium oxide solution, and calcium hydroxide solution reacts i.e. forming salt with acid, thus by harmful nitrogen oxides and sulphur oxygen in flue gas
Compound is adsorbed.There can be the harmful substances such as some heavy metal elements in flue gas simultaneously, by being arranged in primary adsorption room
Active carbon particle, these harmful elements are adsorbed.It is entered in secondary absorption room in flue gas, remaining steam in flue gas
(also including solution) is further oxidized calcisphere adsorption, to play dry purpose to flue gas.
3, the harmful elements such as heavy metal in medical flying ash are dissolved into pure water by supercritical water reaction, and are uniformly released
It is put into arc in filter plate, by high speed rotation, is separated solution and solid burning ash using centrifugal force.Work as liquid
When arrival in outer filter plate inner membrance, due to the inner membrance be it is non-penetrating, fluid preservation in the position, passes through rotation at this time
Turn for the alkaline matters such as calcium hydroxide to be discharged into solution, calcium hydroxide reacts generation with harmful elements such as heavy metals in solution
Precipitating pumps inner membrance at this time and continues high speed rotation, to precipitating be separated with processing water, the water after realizing supercritical water treatment
It is not contaminated.
Pass through the interior filter plate of setting specific structure (coaxial, hollow hemisphere body, interior accessibke porosity, and film is set in outer arc)
Cooperate with outer filter plate and inner membrance, two steps filtered and the reaction between the filtering of two steps is completed during same,
To greatly improve the treatment effeciency of processing water.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of medical waste treatment device of the present invention.
Wherein: 1- incinerator, 11- incinerator outlet flue, 12- incinerator ash hole, 2- mixing tube, 21- carbonated drink spray head,
22- ozone spray head, 23- contraction mouth, 3- primary adsorption room, 31- calcium oxide particle, 32- active carbon particle, 4- secondary absorption room,
41- aoxidizes calcisphere, 42- secondary absorption chamber inlet, and 43- handles exhanst gas outlet, 5- critical reaction chamber, 51- pure water, 52- heating
Stick, 53- gas siphunculus, 531- air pump, 54- pure water siphunculus, 541- water pump, the outlet of 55- reaction chamber, 6- disengagement chamber, 61- arc
Interior filter plate, the outer filter plate inner membrance of 62-, the outer filter plate of 63- arc, 64- support shaft, 65- handle water out.
Specific embodiment
Embodiment 1
A kind of medical waste substance treating method, the processing method use medical waste treatment device, and the medical treatment is useless
Gurry processing unit includes incinerator, mixing tube, primary adsorption room, secondary absorption room, critical reaction chamber and disengagement chamber.
The incinerator includes burning stove outer covering, incinerator outlet flue and incinerator ash hole, the burning stove outer covering to be in
Upper hollow cylindrical body lower hopper shape structure setting, is provided with porous plate, the porous plate is used between the upper
The burning ash that top incinerated matter generates is drained into lower part, the incinerator cover top portion is provided with incinerator outlet flue, at it
Lower hopper shape structure bottom end forms incinerator ash hole.
The mixing tube includes shell, carbonated drink spray head, ozone spray head and contraction mouth, and the shell is that vertical tubular structure is set
It sets, shell top is provided with the contraction mouth of upside down funnel shape, the shell lower part is connected with the incinerator outlet flue, institute
It states shell and tube sides portion and is respectively arranged with carbonated drink spray head and ozone spray head, it is mixed to be respectively used to the inside of mixing tube to spray carbonated drink obliquely
Close object and ozone.
The primary adsorption room includes level-one chamber enclosure, level-one chamber inlet, the outlet of level-one room and calcium oxide particle and work
Property charcoal particle；The calcium oxide particle and active carbon particle, which uniformly gather, to be distributed in the level-one chamber enclosure, outside level-one room
Shell bottom side is provided with level-one chamber inlet, and shell-side top is provided with the outlet of level-one room outside level-one room；The level-one room enters
Mouth is connected with the contraction mouth top.
The secondary absorption room includes second level chamber enclosure, secondary absorption chamber inlet, processing exhanst gas outlet and oxidation calcisphere；Institute
It states secondary absorption chamber inlet to be arranged in secondary chamber outer casing bottom, and is connected with level-one room outlet, the processing flue gas
Outlet is arranged in secondary chamber cover top portion side, and the oxidation calcisphere is uniformly distributed in the second level chamber enclosure.
The critical reaction chamber include reaction chamber enclosure, pure water, heating rod, gas siphunculus, air pump, pure water siphunculus,
Water pump, reaction chamber entrance and reaction chamber outlet；Reaction chamber entrance setting reaction chamber cover top portion and with the incinerator
Ash hole is connected, and is recessed downwards in the reaction chamber outer casing bottom and forms the reaction chamber outlet, in the reaction chamber enclosure
Interior bottom is vertically arranged with multiple heating rods, and reaction chamber top side wall is provided with gas siphunculus, sets on the gas siphunculus
It is equipped with air pump, the gas siphunculus and air pump are used to adjust critical reaction chamber internal pressure by the injection and extraction of gas,
Reaction chamber side wall middle and upper part is provided with pure water siphunculus and water pump, the pure water siphunculus and water pump are used for reaction chamber enclosure
Inside injection pure water, the pure water is set to reaction chamber interior of shell, and the height of pure water is that reaction chamber enclosure is high
The 52% of degree.
The disengagement chamber includes filter plate, outer filter plate inner membrance, the outer filter plate of arc, support in separation chamber enclosure, arc
Axis, disengagement chamber entrance and processing water out；The separation chamber enclosure is hollow rectangular parallelepiped structure, is provided with point in its center of top
From chamber entrance, the disengagement chamber entrance is connected with reaction chamber outlet, sets gradually immediately below the disengagement chamber entrance
There is the outer filter plate of filter plate in the arc of the hollow hemisphere bodily form, outer filter plate inner membrance and arc, the outer filter plate inner membrance is close to
In inside filter plate, filter plate bottom is vertically arranged with support outside filter plate in the arc and arc outside the arc
Axis, filter plate and the outer filter plate of arc are densely covered porous plate in the arc, the support shaft bottom by bearing with it is described
The rotation of disengagement chamber outer casing bottom is affixed, and filter plate and the outer filter plate of arc can be rotated by axis of support shaft in the arc, institute
Support shaft is stated as hollow structure setting, the hollow structure is being provided with out between filter plate outside filter plate in arc and arc
Mouthful, for by alkaline matter by being placed to inside support shaft in arc outside filter plate and arc between filter plate；At described point
Chamber enclosure side bottom is provided with processing water out.
The support shaft is detachable.
The medical waste substance treating method includes the following steps.
(1) Biohazard Waste is placed in incinerator and is burned, the flue gas for burning generation passes through incinerator outlet flue
It enters in mixing tube, the burning ash for burning generation is entered in critical reaction chamber by incinerator ash hole.
(2) flue gas for burning generation, which enters in mixing tube, moves upwards, and starts carbonated drink spray head and ozone spray head, to
Steam water interface and ozone are sprayed in flue gas, so that flue gas brings moisture into uphill process, while ozone is to therein low
Valence nitrogen oxides are the nitrogen oxides of high price, and the water adsorption dissolution being injected into.
(3) flue gas improves gas pressure by contraction mouth and accelerates into primary adsorption room, aqueous sulphur in flue gas
Oxide and the aqueous nitrogen oxides being oxidized are reacted with calcium oxide particle, while the heavy metal element in flue gas is oxidized calcium
Particle and active carbon particle absorption.
(4) flue gas enters in secondary absorption room from primary adsorption room, and the calcium oxide particle in secondary absorption room is by flue gas
The water adsorption of middle remnants, then by processing exhanst gas outlet will treated flue gas emission into air.
(5) burning ash is entered in critical reaction chamber by incinerator ash hole, and critical reaction is intracavitary to be provided with pure water,
Start and the intracavitary pressure of critical reaction is adjusted by gas pipeline and air pump while heating rod heats pure water, so that critical
Pressure and temperature in reaction chamber reaches the critical pressure and critical-temperature of supercritical water so that pure water by burning ash a huge sum of money
Belong to element dissolution.
The intracavitary pressure of the critical reaction is 22.2MPa, and the temperature of pure water is 375 DEG C.
(6) reaction chamber outlet is opened, solidliquid mixture is discharged into disengagement chamber, while opening motor and making mistake in arc
Filter plate and the outer filter plate of arc are around support shaft high speed rotation, so that solid ash content is maintained at liquid separation in filter plate in arc
In to arc outside filter plate and arc between filter plate, the opening being then turned in support shaft releases calcium hydroxide, continues high
After a certain period of time, outer filter plate inner membrance is extracted away for speed rotation, continues high speed rotation, thus the heavy metal that will be obtained after reaction
Alkaloid substance is maintained in the outer filter plate of arc, and the processing water after handling is split into the disengagement chamber outside the outer filter plate of arc
In shell, then pass through processing water out discharge.
The continuation high speed rotation certain time is specially 3.2min.
After filter plate rotation outside filter plate in arc and arc, support shaft top opening is opened, by solid ash content
It is discharged downwards by support shaft, is then led to the heavy metal alkaloid substance outside arc in filter plate by opening support shaft side mouth
Cross discharge downwards inside support shaft.
Embodiment 2
A kind of medical waste substance treating method, the processing method use medical waste treatment device, and the medical treatment is useless
Gurry processing unit includes incinerator, mixing tube, primary adsorption room, secondary absorption room, critical reaction chamber and disengagement chamber.
The incinerator includes burning stove outer covering, incinerator outlet flue and incinerator ash hole, the burning stove outer covering to be in
Upper hollow cylindrical body lower hopper shape structure setting, is provided with porous plate, the porous plate is used between the upper
The burning ash that top incinerated matter generates is drained into lower part, the incinerator cover top portion is provided with incinerator outlet flue, at it
Lower hopper shape structure bottom end forms incinerator ash hole.
The mixing tube includes shell, carbonated drink spray head, ozone spray head and contraction mouth, and the shell is that vertical tubular structure is set
It sets, shell top is provided with the contraction mouth of upside down funnel shape, the shell lower part is connected with the incinerator outlet flue, institute
It states shell and tube sides portion and is respectively arranged with carbonated drink spray head and ozone spray head, it is mixed to be respectively used to the inside of mixing tube to spray carbonated drink obliquely
Close object and ozone.
The primary adsorption room includes level-one chamber enclosure, level-one chamber inlet, the outlet of level-one room and calcium oxide particle and work
Property charcoal particle；The calcium oxide particle and active carbon particle, which uniformly gather, to be distributed in the level-one chamber enclosure, outside level-one room
Shell bottom side is provided with level-one chamber inlet, and shell-side top is provided with the outlet of level-one room outside level-one room；The level-one room enters
Mouth is connected with the contraction mouth top.
The secondary absorption room includes second level chamber enclosure, secondary absorption chamber inlet, processing exhanst gas outlet and oxidation calcisphere；Institute
It states secondary absorption chamber inlet to be arranged in secondary chamber outer casing bottom, and is connected with level-one room outlet, the processing flue gas
Outlet is arranged in secondary chamber cover top portion side, and the oxidation calcisphere is uniformly distributed in the second level chamber enclosure.
The critical reaction chamber include reaction chamber enclosure, pure water, heating rod, gas siphunculus, air pump, pure water siphunculus,
Water pump, reaction chamber entrance and reaction chamber outlet；Reaction chamber entrance setting reaction chamber cover top portion and with the incinerator
Ash hole is connected, and is recessed downwards in the reaction chamber outer casing bottom and forms the reaction chamber outlet, in the reaction chamber enclosure
Interior bottom is vertically arranged with multiple heating rods, and reaction chamber top side wall is provided with gas siphunculus, sets on the gas siphunculus
It is equipped with air pump, the gas siphunculus and air pump are used to adjust critical reaction chamber internal pressure by the injection and extraction of gas,
Reaction chamber side wall middle and upper part is provided with pure water siphunculus and water pump, the pure water siphunculus and water pump are used for reaction chamber enclosure
Inside injection pure water, the pure water is set to reaction chamber interior of shell, and the height of pure water is that reaction chamber enclosure is high
The 58% of degree.
The disengagement chamber includes filter plate, outer filter plate inner membrance, the outer filter plate of arc, support in separation chamber enclosure, arc
Axis, disengagement chamber entrance and processing water out；The separation chamber enclosure is hollow rectangular parallelepiped structure, is provided with point in its center of top
From chamber entrance, the disengagement chamber entrance is connected with reaction chamber outlet, sets gradually immediately below the disengagement chamber entrance
There is the outer filter plate of filter plate in the arc of the hollow hemisphere bodily form, outer filter plate inner membrance and arc, the outer filter plate inner membrance is close to
In inside filter plate, filter plate bottom is vertically arranged with support outside filter plate in the arc and arc outside the arc
Axis, filter plate and the outer filter plate of arc are densely covered porous plate in the arc, the support shaft bottom by bearing with it is described
The rotation of disengagement chamber outer casing bottom is affixed, and filter plate and the outer filter plate of arc can be rotated by axis of support shaft in the arc, institute
Support shaft is stated as hollow structure setting, the hollow structure is being provided with out between filter plate outside filter plate in arc and arc
Mouthful, for by alkaline matter by being placed to inside support shaft in arc outside filter plate and arc between filter plate；At described point
Chamber enclosure side bottom is provided with processing water out.
The support shaft is detachable.
The medical waste substance treating method includes the following steps.
(1) Biohazard Waste is placed in incinerator and is burned, the flue gas for burning generation passes through incinerator outlet flue
It enters in mixing tube, the burning ash for burning generation is entered in critical reaction chamber by incinerator ash hole.
(2) flue gas for burning generation, which enters in mixing tube, moves upwards, and starts carbonated drink spray head and ozone spray head, to
Steam water interface and ozone are sprayed in flue gas, so that flue gas brings moisture into uphill process, while ozone is to therein low
Valence nitrogen oxides are the nitrogen oxides of high price, and the water adsorption dissolution being injected into.
(3) flue gas improves gas pressure by contraction mouth and accelerates into primary adsorption room, aqueous sulphur in flue gas
Oxide and the aqueous nitrogen oxides being oxidized are reacted with calcium oxide particle, while the heavy metal element in flue gas is oxidized calcium
Particle and active carbon particle absorption.
(4) flue gas enters in secondary absorption room from primary adsorption room, and the calcium oxide particle in secondary absorption room is by flue gas
The water adsorption of middle remnants, then by processing exhanst gas outlet will treated flue gas emission into air.
(5) burning ash is entered in critical reaction chamber by incinerator ash hole, and critical reaction is intracavitary to be provided with pure water,
Start and the intracavitary pressure of critical reaction is adjusted by gas pipeline and air pump while heating rod heats pure water, so that critical
Pressure and temperature in reaction chamber reaches the critical pressure and critical-temperature of supercritical water so that pure water by burning ash a huge sum of money
Belong to element dissolution.
The intracavitary pressure of the critical reaction is 22.1MPa, and the temperature of pure water is 374 DEG C.
(6) reaction chamber outlet is opened, solidliquid mixture is discharged into disengagement chamber, while opening motor and making mistake in arc
Filter plate and the outer filter plate of arc are around support shaft high speed rotation, so that solid ash content is maintained at liquid separation in filter plate in arc
In to arc outside filter plate and arc between filter plate, the opening being then turned in support shaft releases sodium hydroxide, continues high
After a certain period of time, outer filter plate inner membrance is extracted away for speed rotation, continues high speed rotation, thus the heavy metal that will be obtained after reaction
Alkaloid substance is maintained in the outer filter plate of arc, and the processing water after handling is split into the disengagement chamber outside the outer filter plate of arc
In shell, then pass through processing water out discharge.
The continuation high speed rotation certain time is specially 3.5min.
After filter plate rotation outside filter plate in arc and arc, support shaft top opening is opened, by solid ash content
It is discharged downwards by support shaft, is then led to the heavy metal alkaloid substance outside arc in filter plate by opening support shaft side mouth
Cross discharge downwards inside support shaft.
Embodiment 3
A kind of medical waste substance treating method, the processing method use medical waste treatment device, and the medical treatment is useless
Gurry processing unit includes incinerator, mixing tube, primary adsorption room, secondary absorption room, critical reaction chamber and disengagement chamber.
The incinerator includes burning stove outer covering, incinerator outlet flue and incinerator ash hole, the burning stove outer covering to be in
Upper hollow cylindrical body lower hopper shape structure setting, is provided with porous plate, the porous plate is used between the upper
The burning ash that top incinerated matter generates is drained into lower part, the incinerator cover top portion is provided with incinerator outlet flue, at it
Lower hopper shape structure bottom end forms incinerator ash hole.
The mixing tube includes shell, carbonated drink spray head, ozone spray head and contraction mouth, and the shell is that vertical tubular structure is set
It sets, shell top is provided with the contraction mouth of upside down funnel shape, the shell lower part is connected with the incinerator outlet flue, institute
It states shell and tube sides portion and is respectively arranged with carbonated drink spray head and ozone spray head, it is mixed to be respectively used to the inside of mixing tube to spray carbonated drink obliquely
Close object and ozone.
The primary adsorption room includes level-one chamber enclosure, level-one chamber inlet, the outlet of level-one room and calcium oxide particle and work
Property charcoal particle；The calcium oxide particle and active carbon particle, which uniformly gather, to be distributed in the level-one chamber enclosure, outside level-one room
Shell bottom side is provided with level-one chamber inlet, and shell-side top is provided with the outlet of level-one room outside level-one room；The level-one room enters
Mouth is connected with the contraction mouth top.
The secondary absorption room includes second level chamber enclosure, secondary absorption chamber inlet, processing exhanst gas outlet and oxidation calcisphere；Institute
It states secondary absorption chamber inlet to be arranged in secondary chamber outer casing bottom, and is connected with level-one room outlet, the processing flue gas
Outlet is arranged in secondary chamber cover top portion side, and the oxidation calcisphere is uniformly distributed in the second level chamber enclosure.
The critical reaction chamber include reaction chamber enclosure, pure water, heating rod, gas siphunculus, air pump, pure water siphunculus,
Water pump, reaction chamber entrance and reaction chamber outlet；Reaction chamber entrance setting reaction chamber cover top portion and with the incinerator
Ash hole is connected, and is recessed downwards in the reaction chamber outer casing bottom and forms the reaction chamber outlet, in the reaction chamber enclosure
Interior bottom is vertically arranged with multiple heating rods, and reaction chamber top side wall is provided with gas siphunculus, sets on the gas siphunculus
It is equipped with air pump, the gas siphunculus and air pump are used to adjust critical reaction chamber internal pressure by the injection and extraction of gas,
Reaction chamber side wall middle and upper part is provided with pure water siphunculus and water pump, the pure water siphunculus and water pump are used for reaction chamber enclosure
Inside injection pure water, the pure water is set to reaction chamber interior of shell, and the height of pure water is that reaction chamber enclosure is high
The 62% of degree.
The disengagement chamber includes filter plate, outer filter plate inner membrance, the outer filter plate of arc, support in separation chamber enclosure, arc
Axis, disengagement chamber entrance and processing water out；The separation chamber enclosure is hollow rectangular parallelepiped structure, is provided with point in its center of top
From chamber entrance, the disengagement chamber entrance is connected with reaction chamber outlet, sets gradually immediately below the disengagement chamber entrance
There is the outer filter plate of filter plate in the arc of the hollow hemisphere bodily form, outer filter plate inner membrance and arc, the outer filter plate inner membrance is close to
In inside filter plate, filter plate bottom is vertically arranged with support outside filter plate in the arc and arc outside the arc
Axis, filter plate and the outer filter plate of arc are densely covered porous plate in the arc, the support shaft bottom by bearing with it is described
The rotation of disengagement chamber outer casing bottom is affixed, and filter plate and the outer filter plate of arc can be rotated by axis of support shaft in the arc, institute
Support shaft is stated as hollow structure setting, the hollow structure is being provided with out between filter plate outside filter plate in arc and arc
Mouthful, for by alkaline matter by being placed to inside support shaft in arc outside filter plate and arc between filter plate；At described point
Chamber enclosure side bottom is provided with processing water out.
The support shaft is detachable.
The medical waste substance treating method includes the following steps.
(1) Biohazard Waste is placed in incinerator and is burned, the flue gas for burning generation passes through incinerator outlet flue
It enters in mixing tube, the burning ash for burning generation is entered in critical reaction chamber by incinerator ash hole.
(2) flue gas for burning generation, which enters in mixing tube, moves upwards, and starts carbonated drink spray head and ozone spray head, to
Steam water interface and ozone are sprayed in flue gas, so that flue gas brings moisture into uphill process, while ozone is to therein low
Valence nitrogen oxides are the nitrogen oxides of high price, and the water adsorption dissolution being injected into.
(3) flue gas improves gas pressure by contraction mouth and accelerates into primary adsorption room, aqueous sulphur in flue gas
Oxide and the aqueous nitrogen oxides being oxidized are reacted with calcium oxide particle, while the heavy metal element in flue gas is oxidized calcium
Particle and active carbon particle absorption.
(4) flue gas enters in secondary absorption room from primary adsorption room, and the calcium oxide particle in secondary absorption room is by flue gas
The water adsorption of middle remnants, then by processing exhanst gas outlet will treated flue gas emission into air.
(5) burning ash is entered in critical reaction chamber by incinerator ash hole, and critical reaction is intracavitary to be provided with pure water,
Start and the intracavitary pressure of critical reaction is adjusted by gas pipeline and air pump while heating rod heats pure water, so that critical
Pressure and temperature in reaction chamber reaches the critical pressure and critical-temperature of supercritical water so that pure water by burning ash a huge sum of money
Belong to element dissolution.
The intracavitary pressure and temperature for forming supercritical water of the critical reaction, specially pressure 22.3MPa, the temperature of pure water
Degree is 374 DEG C.
(6) reaction chamber outlet is opened, solidliquid mixture is discharged into disengagement chamber, while opening motor and making mistake in arc
Filter plate and the outer filter plate of arc are around support shaft high speed rotation, so that solid ash content is maintained at liquid separation in filter plate in arc
In to arc outside filter plate and arc between filter plate, the opening being then turned in support shaft releases potassium hydroxide, continues high
After a certain period of time, outer filter plate inner membrance is extracted away for speed rotation, continues high speed rotation, thus the heavy metal that will be obtained after reaction
Alkaloid substance is maintained in the outer filter plate of arc, and the processing water after handling is split into the disengagement chamber outside the outer filter plate of arc
In shell, then pass through processing water out discharge.
The continuation high speed rotation certain time is specially 3.8min.
After filter plate rotation outside filter plate in arc and arc, support shaft top opening is opened, by solid ash content
It is discharged downwards by support shaft, is then led to the heavy metal alkaloid substance outside arc in filter plate by opening support shaft side mouth
Cross discharge downwards inside support shaft.
Claims (6)
1. a kind of medical waste substance treating method, which is characterized in that the processing method uses medical waste treatment device, institute
Stating medical waste treatment device includes incinerator, mixing tube, primary adsorption room, secondary absorption room, critical reaction chamber and separation
Chamber；
The incinerator includes burning stove outer covering, incinerator outlet flue and incinerator ash hole, the burning stove outer covering to present portion
Hollow cylinder lower hopper shape structure setting, is provided with porous plate between the upper, the porous plate be used for by
The burning ash that portion's incinerated matter generates drains to lower part, the incinerator cover top portion is provided with incinerator outlet flue, in its underpart
Funnel-shaped structure bottom end forms incinerator ash hole；
The mixing tube includes shell, carbonated drink spray head, ozone spray head and contraction mouth, and the shell is vertical tubulose structure setting,
Shell top is provided with the contraction mouth of upside down funnel shape, the shell lower part is connected with the incinerator outlet flue, described
Shell and tube sides portion is respectively arranged with carbonated drink spray head and ozone spray head, is respectively used to spray steam-water mixing obliquely to the inside of mixing tube
Object and ozone；
The primary adsorption room includes level-one chamber enclosure, level-one chamber inlet, the outlet of level-one room and calcium oxide particle and active carbon
Particle；The calcium oxide particle and active carbon particle, which uniformly gather, to be distributed in the level-one chamber enclosure, at level-one chamber enclosure bottom
Portion side is provided with level-one chamber inlet, and shell-side top is provided with the outlet of level-one room outside level-one room；The level-one chamber inlet with
The contraction mouth top is connected；
The secondary absorption room includes second level chamber enclosure, secondary absorption chamber inlet, processing exhanst gas outlet and oxidation calcisphere；Described two
Grade absorption chamber inlet is arranged in secondary chamber outer casing bottom, and is connected with level-one room outlet, the processing exhanst gas outlet
It is arranged in secondary chamber cover top portion side, the oxidation calcisphere is uniformly distributed in the second level chamber enclosure；
The critical reaction chamber include reaction chamber enclosure, pure water, heating rod, gas siphunculus, air pump, pure water siphunculus, water pump,
Reaction chamber entrance and reaction chamber outlet；Reaction chamber entrance setting reaction chamber cover top portion and with the incinerator ash hole
It is connected, is recessed downwards in the reaction chamber outer casing bottom and forms the reaction chamber outlet, the bottom in the reaction chamber enclosure
Multiple heating rods are vertically arranged with, reaction chamber top side wall is provided with gas siphunculus, is provided with gas on the gas siphunculus
Pump, the gas siphunculus and air pump are used to adjust critical reaction chamber internal pressure by the injection and extraction of gas, are reacting
Chamber side wall middle and upper part is provided with pure water siphunculus and water pump, and the pure water siphunculus and water pump are used to infuse to reaction chamber interior of shell
Enter pure water, the pure water is set to reaction chamber interior of shell, and the height of pure water is the 50% of reaction chamber outer cover height
~68%；
The disengagement chamber include separation chamber enclosure, the outer filter plate of filter plate, outer filter plate inner membrance, arc in arc, support shaft, point
From chamber entrance and processing water out；The separation chamber enclosure is hollow rectangular parallelepiped structure, its center of top is provided with disengagement chamber
Entrance, the outlet of the disengagement chamber entrance and the reaction chamber be connected, and is disposed with immediately below the disengagement chamber entrance
The outer filter plate of filter plate, outer filter plate inner membrance and arc, the outer filter plate inner membrance are tightly attached to institute in the arc of the empty hemisphere bodily form
It states inside the outer filter plate of arc, filter plate bottom is vertically arranged with support shaft outside filter plate in the arc and arc, institute
Stating filter plate and the outer filter plate of arc in arc is densely covered porous plate, and the support shaft bottom passes through bearing and the disengagement chamber
Outer casing bottom rotation is affixed, and filter plate and the outer filter plate of arc can be rotated by axis of support shaft in the arc, the support
Axis is hollow structure setting, and the hollow structure is being provided with opening, is being used between filter plate outside filter plate in arc and arc
By alkaline matter by being placed to inside support shaft in arc outside filter plate and arc between filter plate；In the separation chamber enclosure
Side bottom is provided with processing water out；
The medical waste substance treating method includes the following steps:
(1) Biohazard Waste is placed in incinerator and is burned, the flue gas for burning generation is entered by incinerator outlet flue
Into mixing tube, the burning ash for burning generation is entered in critical reaction chamber by incinerator ash hole；
(2) flue gas for burning generation, which enters in mixing tube, moves upwards, and starts carbonated drink spray head and ozone spray head, to flue gas
Middle injection steam water interface and ozone, so that flue gas brings moisture into uphill process, while ozone is to Low-Charged Nitrogen therein
Oxides are the nitrogen oxides of high price, and the water adsorption dissolution being injected into；
(3) flue gas improves gas pressure by contraction mouth and accelerates into primary adsorption room, aqueous sulphur oxidation in flue gas
Object and the aqueous nitrogen oxides being oxidized are reacted with calcium oxide particle, while the heavy metal element in flue gas is oxidized calcium particle
It is adsorbed with active carbon particle；
(4) flue gas enters in secondary absorption room from primary adsorption room, and the calcium oxide particle in secondary absorption room will be residual in flue gas
Remaining water adsorption, then by processing exhanst gas outlet will treated flue gas emission into air；
(5) burning ash is entered in critical reaction chamber by incinerator ash hole, and critical reaction is intracavitary to be provided with pure water, starting
The intracavitary pressure of critical reaction is adjusted by gas pipeline and air pump while heating rod heats pure water, so that critical reaction
Intracavitary pressure and temperature reaches the critical pressure and critical-temperature of supercritical water, so that pure water is first by heavy metal in incineration ash
Element dissolution；
(6) reaction chamber outlet is opened, solidliquid mixture is discharged into disengagement chamber, while opening motor and making filter plate in arc
With filter plate outside arc around support shaft high speed rotation so that solid ash content is maintained in arc in filter plate and liquid is separated to arc
In shape between filter plate and the outer filter plate of arc, the opening being then turned in support shaft releases alkaline matter, continues high speed and revolves
Turn that after a certain period of time, outer filter plate inner membrance is extracted away, continues high speed rotation, thus the heavy metal alkali object that will be obtained after reaction
Matter is maintained in the outer filter plate of arc, and the processing water after handling is split into the separation chamber enclosure outside the outer filter plate of arc
It is interior, then pass through processing water out discharge.
2. medical waste substance treating method according to claim 1, which is characterized in that the intracavitary pressure of the critical reaction
For 22.1MPa, the temperature of pure water is 374 DEG C.
3. -2 described in any item medical waste substance treating methods according to claim 1, which is characterized in that described in step (6)
Continuing high speed rotation certain time is specially 3 ~ 5min.
4. medical waste substance treating method according to claim 3, which is characterized in that when being filtered in arc in step (6)
After plate and the outer filter plate rotation of arc, support shaft top opening is opened, solid ash content is discharged downwards by support shaft, so
The heavy metal alkaloid substance outside arc in filter plate is passed through into discharge downwards inside support shaft by opening support shaft side mouth afterwards.
5. medical waste substance treating method according to claim 1, which is characterized in that basic species described in step (6)
Matter is calcium hydroxide.
6. medical waste substance treating method according to claim 1, which is characterized in that the support shaft is detachable.
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| CN113244704B (en) * | 2021-05-10 | 2022-06-14 | 深圳市真味生物科技有限公司 | High-efficient smog collecting device of electron cigarette |
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| JP3419292B2 (en) * | 1998-01-19 | 2003-06-23 | 株式会社日立製作所 | Waste treatment system |
| CN1923341A (en) * | 2006-08-23 | 2007-03-07 | 浙江大学 | Device and method for coal-burning boiler fume ozone oxidation and simultaneous desulfurization and denitrification |
| CN101259369A (en) * | 2008-04-29 | 2008-09-10 | 北京中科创丰科技有限公司 | Flue gas desulfurization denitration dust removing integrated technique |
| CN101502838B (en) * | 2009-03-05 | 2012-07-25 | 中国科学院生态环境研究中心 | Novel technique for harmless treatment of medical refuse burning flyash |
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Effective date of registration: 20190521 Address after: 262200 Unit 402, Unit 3, Building 14, 57 Nanhuan Road, Zhucheng City, Weifang City, Shandong Province Applicant after: Li Jianguo Address before: 266555 Tengjuntaide Medical Equipment Co., Ltd. No. 2 Wuyishan Road, Huangdao District, Qingdao City, Shandong Province Applicant before: Nie Fengling |
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