CN109647093B - Gas condenser and environment-friendly air dust removal device - Google Patents

Gas condenser and environment-friendly air dust removal device Download PDF

Info

Publication number
CN109647093B
CN109647093B CN201910095380.4A CN201910095380A CN109647093B CN 109647093 B CN109647093 B CN 109647093B CN 201910095380 A CN201910095380 A CN 201910095380A CN 109647093 B CN109647093 B CN 109647093B
Authority
CN
China
Prior art keywords
lnq
flf
pipe
gas condenser
gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201910095380.4A
Other languages
Chinese (zh)
Other versions
CN109647093A (en
Inventor
聂新明
赵新生
陈斯
王勋
田亚平
田康振
杨增汪
乔学斌
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jiangsu Normal University
Original Assignee
Jiangsu Normal University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Jiangsu Normal University filed Critical Jiangsu Normal University
Priority to CN201910095380.4A priority Critical patent/CN109647093B/en
Publication of CN109647093A publication Critical patent/CN109647093A/en
Application granted granted Critical
Publication of CN109647093B publication Critical patent/CN109647093B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • 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
    • B01D53/002—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 by condensation
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B21/00—Machines, plants or systems, using electric or magnetic effects
    • F25B21/02—Machines, plants or systems, using electric or magnetic effects using Peltier effect; using Nernst-Ettinghausen effect
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/02—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point using Joule-Thompson effect; using vortex effect
    • F25B9/04—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point using Joule-Thompson effect; using vortex effect using vortex effect
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28B—STEAM OR VAPOUR CONDENSERS
    • F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
    • F28B1/02—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using water or other liquid as the cooling medium
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28B—STEAM OR VAPOUR CONDENSERS
    • F28B9/00—Auxiliary systems, arrangements, or devices

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

The gas condenser comprises an upper cavity (LNQ-SQ), a lower cavity (LNQ-XQ), an air inlet pipe (LNQ-JG), an air outlet pipe (LNQ-PQG), a heat exchanger, a balance air pipe (LNQ-QG2), a second separation valve (FLF2), a water outlet pipe (LNQ-PSG) and an air exhaust pump (B2). The environment-friendly air dust removal device is provided with the gas condenser. The invention has simple structure, low energy consumption, high efficiency and good effect, and creates a new technical idea.

Description

Gas condenser and environment-friendly air dust removal device
Technical Field
The invention relates to gas cleaning, in particular to a gas condenser and an environment-friendly air dust removal device.
Background
Gas dust removal is called dust removal for short. Process for removing dust-donating materials suspended in gas in the chemical, fuel, metallurgical and other industries, gases containing a large amount of dust are often produced, and the dust must be removed so that the subsequent production process can be smoothly continued. For example, in the production of sulfuric acid by the contact method, if fine particles of arsenic, selenium, or the like suspended in a raw material gas are not removed, the catalyst is poisoned. Except that the factory meets the requirement of industrial production, the dust removal is also to recycle, labor protection, urban and rural sanitation, crop protection and the like, for example, the waste gas discharged by some industrial enterprises should be subjected to certain degree of dust removal without directly releasing people into the atmosphere.
Environmental protection generally refers to the collective name of various actions that human beings take to solve real or potential environmental problems, coordinate the relationship between human beings and the environment, protect the living environment of human beings, and guarantee the sustainable development of the economy and society. The environmental protection relates to the problems that private mining (mining) is incapable of cutting trees, the waste water is incapable of being discharged randomly (sewage) and discharging randomly (foul air), the grazing cannot be performed excessively, the wastefulness cannot be performed excessively, natural resources cannot be developed excessively, the ecological balance of the nature cannot be damaged, and the like. The environment protection needs to remove dust from the flue gas generated in the production process, and the equipment for separating the dust from the flue gas is called a dust remover. The existing dust collectors have various types and also have various defects, such as incapability of adapting to high-temperature flue gas (such as a bag-type dust collector), high maintenance cost (such as an electrostatic dust collector) and low dust collection efficiency (such as a cyclone dust collector).
The prior art dust removal methods comprise gravity settling, centrifugal separation, filtration [ T-method ], liquid washing (wet method), electrostatic, sound wave and ultrasonic, and the like, and the methods have advantages and disadvantages respectively.
Disclosure of Invention
In view of the defects or shortcomings in the prior art, the invention provides a gas condenser and an environment-friendly air dust removal device, and creates a new idea.
1. The gas condenser comprises an upper cavity (LNQ-SQ), a lower cavity (LNQ-XQ), an air inlet pipe (LNQ-JG), an air outlet pipe (LNQ-PQG), a heat exchanger, a balance air pipe (LNQ-QG2), a second separation valve (FLF2), a water outlet pipe (LNQ-PSG) and an air exhaust pump (B2);
in the gas condenser: the upper chamber (LNQ-SQ) is filled with cooling water for cooling;
in the gas condenser: the cavity of the lower cavity (LNQ-XQ) is not filled with water, a gas space is reserved, the gas space is communicated with the atmosphere through a balance gas pipe (LNQ-QG2), and the opening position of the balance gas pipe (LNQ-QG2) in the atmosphere is higher than the highest point of water communicated with the upper cavity (LNQ-SQ);
the second separation valve (FLF2) of the gas condenser is a water-gas separation valve (FLF) which only releases water and does not release gas;
the water-gas separation valve (FLF) comprises a water outlet pipe (FLF-CSG), a conical cavity (FLF-ZXQ), a heavy ball (FLF-ZQ) and a floating ball (FLF-FQ);
in the second separation valve (FLF2) of the gas condenser: the conical cavity (FLF-ZXQ) is arranged in an axis-vertical mode, the large end of the conical cavity (FLF-ZXQ) is arranged above, and the small end of the conical cavity (FLF-ZXQ) is arranged below;
in the second separation valve (FLF2) of the gas condenser: the density of the heavy ball (FLF-ZQ) is larger than that of water in the application environment;
in the second separation valve (FLF2) of the gas condenser: the density of the floating ball (FLF-FQ) is less than that of water in an application environment;
in the second separation valve (FLF2) of the gas condenser: the lower end of the conical cavity (FLF-ZXQ) is connected with the highest point of the water outlet pipe (FLF-CSG); in the second separation valve (FLF2) of the gas condenser: the diameter of the heavy ball (FLF-ZQ) is smaller than the large end of the conical cavity (FLF-ZXQ), and the diameter of the heavy ball (FLF-ZQ) is larger than the small end of the conical cavity (FLF-ZXQ);
in the second separation valve (FLF2) of the gas condenser: a heavy ball (FLF-ZQ) device is arranged in the conical cavity (FLF-ZXQ);
in the second separation valve (FLF2) of the gas condenser: the floating ball (FLF-FQ) is connected with the heavy ball (FLF-ZQ) through a flexible wire, when the floating ball (FLF-FQ) is floated by water in the cavity of the water-gas separation valve (FLF), the heavy ball (FLF-ZQ) is pulled up by the floating ball (FLF-FQ), the lower end of the conical cavity (FLF-ZXQ) is released, the water is discharged through the upper end of the conical cavity (FLF-ZXQ), the lower end of the conical cavity (FLF-ZXQ) and the water outlet pipe (FLF-CSG), when the water level lowers the heavy ball (FLF-ZQ) and falls on the lower end of the conical cavity (FLF-ZXQ) because of gravity, the lower end of the conical cavity (FLF-ZXQ) is closed and does not discharge water any more, since the floating ball (FLF-FQ) is connected with the heavy ball (FLF-ZQ) through a flexible wire, when the water surface descends to the height of the heavy ball and the line is lengthened, the lower end of the conical cavity (FLF-ZXQ) is closed, so that the gas cannot be discharged;
the upper end of a conical cavity (FLF-ZXQ) of a second separation valve (FLF2) of the gas condenser is communicated with the lower cavity (LNQ-XQ), the lower end of the conical cavity (FLF-ZXQ) of the second separation valve (FLF2) is higher than the bottom of the lower cavity (LNQ-XQ), and the lowest point of an outlet of a water outlet pipe (FLF-CSG) of a second separation valve (FLF2) is higher than the bottom of the lower cavity (LNQ-XQ);
the heat exchanger of the gas condenser is composed of a plurality of heat exchange tubes (LNQ-HG);
the heat exchange tube (LNQ-HG) of the gas condenser comprises a first tube (LNQ-HG-1), a second tube (LNQ-HG-2), a third tube (LNQ-HG-3), a fourth tube (LNQ-HG-4), a fifth tube (LNQ-HG-5), a sixth tube (LNQ-HG-6) and a seventh tube (LNQ-HG-7);
in the heat exchange tube (LNQ-HG) of the gas condenser: the first pipe (LNQ-HG-1) is arranged in a mode that the axis is horizontal;
in the heat exchange tube (LNQ-HG) of the gas condenser: the second pipe (LNQ-HG-1) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the third pipe (LNQ-HG-3) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the fourth pipe (LNQ-HG-4) is arranged in a mode that the axis is horizontal;
in the heat exchange tube (LNQ-HG) of the gas condenser: the fifth pipe (LNQ-HG-5) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the sixth pipe (LNQ-HG-6) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the seventh pipe (LNQ-HG-7) is arranged in a mode that the axis is horizontal;
in the heat exchange tube (LNQ-HG) of the gas condenser: the lower end of the second pipe (LNQ-HG-1) is open to the outside;
in the heat exchange tube (LNQ-HG) of the gas condenser: the lower end of the sixth pipe (LNQ-HG-6) has an opening to the outside;
in the heat exchange tube (LNQ-HG) of the gas condenser: the left end of the first pipe (LNQ-HG-1), the lower end of the third pipe (LNQ-HG-3) and the upper end of the second pipe (LNQ-HG-2) are connected and communicated;
in the heat exchange tube (LNQ-HG) of the gas condenser: the right end of the seventh pipe (LNQ-HG-7), the lower end of the fifth pipe (LNQ-HG-5) and the upper end of the sixth pipe (LNQ-HG-6) are connected and communicated;
in the heat exchange tube (LNQ-HG) of the gas condenser: the upper end of the third pipe (LNQ-HG-3) is connected and communicated with the right end of the fourth pipe (LNQ-HG-4);
in the heat exchange tube (LNQ-HG) of the gas condenser: the upper end of the fifth pipe (LNQ-HG-5) is connected and communicated with the left end of the fourth pipe (LNQ-HG-4);
the heat exchange tubes (LNQ-HG) of the gas condenser form a heat exchanger by a combination method that two adjacent heat exchange tubes (LNQ-HG) are named as a left heat exchange tube and a right heat exchange tube, and a first tube (LNQ-HG-1) of the left heat exchange tube is connected and communicated with a seventh tube (LNQ-HG-7) of the right heat exchange tube;
in the gas condenser: the horizontal positions of the openings of the lower ends of the second tubes (LNQ-HG-1) and the lower ends of the sixth tubes (LNQ-HG-6) of all the heat exchange tubes (LNQ-HG) of the heat exchanger are lower than the upper end of the conical cavity (FLF-ZXQ) of the second separation valve (FLF 2);
in the gas condenser: the openings of the lower ends of the second tubes (LNQ-HG-1) and the lower ends of the sixth tubes (LNQ-HG-6) of all heat exchange tubes (LNQ-HG) of the heat exchanger are in the lower chamber (LNQ-XQ);
in the gas condenser: opening of lower end of second tube (LNQ-HG-1) of all heat exchange tubes (LNQ-HG) of heat exchanger and sixth tube (LNQ-HG-6)
In the gas condenser: an air inlet of an exhaust pump (B2) is communicated with a seventh pipe (LNQ-HG-7) of the leftmost heat exchange pipe (LNQ-HG), an air outlet of the exhaust pump (B2) is communicated with an air inlet of an exhaust pipe (LNQ-PQG), an air inlet pipe (LNQ-JG) is communicated with a first pipe (LNQ-HG-1) of the rightmost heat exchange pipe (LNQ-HG), the gas passes through the heat exchanger and is cooled, water droplets contained in the gas are condensed into water drops, the water drops fall into a lower cavity (LNQ-XQ), and after the water in the lower cavity (LNQ-XQ) reaches a certain water level, a part of the water drops is discharged and retained through a second separation valve (FLF2) to remove the water component contained in the gas.
2. A gas condenser as set forth in claim 1, characterized in that: the upper cavity (LNQ-SQ) is a square cavity.
3. A gas condenser as set forth in claim 1, characterized in that: the upper chamber (LNQ-SQ) has a temperature sensor therein.
4. A gas condenser as set forth in claim 1, characterized in that: the lower cavity (LNQ-XQ) has a temperature sensor therein.
5. A gas condenser as set forth in claim 1, characterized in that: the exhaust pipes (LNQ-PQG) are made of metal.
6. A gas condenser as set forth in claim 1, characterized in that: the exhaust pipes (LNQ-PQG) are made of plastic.
7. A gas condenser as set forth in claim 1, characterized in that: the material of the balance air pipe (LNQ-QG2) is plastic.
8. A gas condenser as set forth in claim 1, characterized in that: the balance air pipe (LNQ-QG2) is made of metal.
9. Environmental protection air dust collector, its characterized in that: the gas condenser described in claim 1.
Technical principle and beneficial effect thereof.
The invention has simple structure, low energy consumption, high efficiency and good effect, and creates a new technical idea.
Drawings
Fig. 1 is a block diagram of example 1, which shows a method of designing a gas purification system for an application environment of the present invention.
FIG. 2 is a structural view of embodiment 2.
Fig. 3 is a structural view of a gas condenser of embodiment 2.
FIG. 4 is a structural view of a heat exchange tube (LNQ-HG) of the gas condenser of example 2.
Fig. 5 is a structural view of a water gas separation valve (FLF) of the gas condenser of embodiment 2.
FIG. 6 is a block diagram of embodiment 3.
Fig. 7 is a structural view of the rotor (1) of the mechanical rotary bubble generator of embodiment 3.
FIG. 8 is a structural view of the container (2) of the mechanical rotary type bubble generator of example 3.
Fig. 9 is a structural view of the cover (3) of the mechanical rotary type bubble generator of embodiment 3.
Fig. 10 is a structural view of a bearing (4) of the mechanical rotary bubble generator of embodiment 3.
Fig. 11 is a schematic view of the motor (5) of the mechanical rotary type bubble generator of embodiment 3.
Fig. 12 is a schematic view of the assembly of the mechanical rotary type bubble generator of embodiment 3. Wherein 6 is a rivet connecting the bearing (4) and the rotor (1).
Fig. 13 is an overall schematic view of the mechanical rotary type bubble generator of embodiment 3.
DETAILED DESCRIPTION OF EMBODIMENT (S) OF INVENTION
Embodiment 1, a system of gaseous dust removal, its characterized in that: comprises a gas cooling container, a steam generator, a gas mixing container and a gas condenser;
the gas cooling container is used for reducing the temperature of the gas;
the steam generator is used for generating steam;
the gas to be treated is cooled by the gas cooling container to become cooled gas, the cooled gas enters the gas mixer to be mixed with the water vapor to form mixed gas, and water vapor molecules collide with dust in the cooled gas and then are cooled and attached to the dust to form rain nuclei;
and the mixed gas enters a gas condenser, and after cooling, the water vapor is further attached to a rain core to form water drops to form rainfall or condensation, and the rainfall or condensation takes away dust particles.
Example 2, as shown in fig. 2-5, a gas dedusting system, characterized by: the device is composed of a refrigerating container (R1), a heating container (R2), a mixing container (R3), a gas condenser, a gas inlet pipeline (JQG) and a refrigerating and heating device (ZLQ-3);
the refrigeration container (R1) is provided with a partition plate (R1-GLB), the partition plate (R1-GLB) divides the refrigeration container (R1) into a first cavity and a second cavity, a connecting hole (R1-LJK) is formed below the partition plate (R1-GLB), and the first cavity is communicated with the second cavity through the connecting hole (R1-LJK); the refrigeration container (R1) is partially filled with cold water, and the water level of the cold water in the refrigeration container (R1) is lower than the top end of the isolation plate (R1-GLB); the refrigeration container (R1) is also provided with a drain pipe (R1-PWG) and a drain valve (R1-PWF), the drain pipe (R1-PWG) is communicated with the bottom of the first cavity, and the drain valve (R1-PWF) is positioned on the drain pipe (R1-PWG) and is used for controlling the discharge of sediment at the bottom of the refrigeration container (R1); an air inlet pipeline (JQG) penetrates through the wall of the refrigeration container (R1) and enters cold water in the first cavity, the opening of the air inlet pipeline (JQG) is higher than the connecting hole (R1-LJK), and the opening of the air inlet pipeline (JQG) is higher than the sewage discharge pipe (R1-PWG);
the interior of the heating container (R2) is filled with hot water;
the mixing container (R3) is internally provided with a stirrer (JBQ), and the stirrer (JBQ) is driven by a motor;
a first separation valve (FLF1) is arranged in the mixing container (R3);
a first separating valve (FLF1) of the mixing container (R3) is positioned at the bottom of the mixing container (R3) and is used for discharging water at the bottom of the mixing container (R3); the first separating valve (FLF1) of the mixing vessel (R3) is a water-gas separating valve (FLF) releasing only water and no gas;
the water-gas separation valve (FLF) comprises a water outlet pipe (FLF-CSG), a conical cavity (FLF-ZXQ), a heavy ball (FLF-ZQ) and a floating ball (FLF-FQ);
in the water-gas separation valve (FLF): the conical cavity (FLF-ZXQ) is arranged in an axis-vertical mode, the large end of the conical cavity (FLF-ZXQ) is arranged above, and the small end of the conical cavity (FLF-ZXQ) is arranged below;
in the water-gas separation valve (FLF): the density of the heavy ball (FLF-ZQ) is larger than that of water in the application environment;
in the water-gas separation valve (FLF): the density of the floating ball (FLF-FQ) is less than that of water in an application environment;
in the water-gas separation valve (FLF): the lower end of the conical cavity (FLF-ZXQ) is connected with the highest point of the water outlet pipe (FLF-CSG);
in the water-gas separation valve (FLF): the diameter of the heavy ball (FLF-ZQ) is smaller than the large end of the conical cavity (FLF-ZXQ), and the diameter of the heavy ball (FLF-ZQ) is larger than the small end of the conical cavity (FLF-ZXQ);
in the water-gas separation valve (FLF): a heavy ball (FLF-ZQ) device is arranged in the conical cavity (FLF-ZXQ);
in the water-gas separation valve (FLF): the floating ball (FLF-FQ) is connected with the heavy ball (FLF-ZQ) through a flexible wire, when the floating ball (FLF-FQ) is floated by water in the cavity of the water-gas separation valve (FLF), the heavy ball (FLF-ZQ) is pulled up by the floating ball (FLF-FQ), the lower end of the conical cavity (FLF-ZXQ) is released, the water is discharged through the upper end of the conical cavity (FLF-ZXQ), the lower end of the conical cavity (FLF-ZXQ) and the water outlet pipe (FLF-CSG), when the water level lowers the heavy ball (FLF-ZQ) and falls on the lower end of the conical cavity (FLF-ZXQ) because of gravity, the lower end of the conical cavity (FLF-ZXQ) is closed and does not discharge water any more, since the floating ball (FLF-FQ) is connected with the heavy ball (FLF-ZQ) through a flexible wire, when the water surface descends to the height of the heavy ball and the line is lengthened, the lower end of the conical cavity (FLF-ZXQ) is closed, so that the gas cannot be discharged;
the upper end of a conical cavity (FLF-ZXQ) of a first separation valve (FLF1) of the mixing container (R3) is communicated with a lower cavity (LNQ-XQ), the lower end of the conical cavity (FLF-ZXQ) of the first separation valve (FLF1) is higher than the bottom of the lower cavity (LNQ-XQ), and the lowest point of an outlet of a water outlet pipe (FLF-CSG) of the first separation valve (FLF1) is higher than the bottom of the lower cavity (LNQ-XQ);
the refrigerating and heating device (ZLQ-3) is provided with a heating end and a refrigerating end, the refrigerating end of the refrigerating and heating device (ZLQ-3) is connected with the refrigerating container (R1) and used for cooling cold water in the refrigerating container (R1), and the heating end of the refrigerating and heating device (ZLQ-3) is connected with the heating container (R1) and used for heating hot water in the heating container (R2);
the top of the refrigeration container (R1) is communicated with the top of the mixing container (R3) through a first heat insulation pipe (GRG1), a first check valve (DXF1) is arranged on the pipeline of the first heat insulation pipe (GRG1), and the gas in the mixing container (R3) cannot flow back to the refrigeration container (R1);
the side wall above the water surface on the left side of the heating container (R2) is communicated with the wall on the right side of the mixing container (R3) through a second heat insulation pipe (GRG 2);
the water outlet pipe of the first separating valve (FLF1) of the heating container (R2) is communicated with the part below the water surface of the heating container (R2) through a third heat-insulating pipe (GRG 3);
the gas condenser comprises an upper cavity (LNQ-SQ), a lower cavity (LNQ-XQ), an air inlet pipe (LNQ-JG), an air outlet pipe (LNQ-PQG), a heat exchanger, a balance air pipe (LNQ-QG2), a second separation valve (FLF2), a water outlet pipe (LNQ-PSG) and an air exhaust pump (B2);
in the gas condenser: the upper chamber (LNQ-SQ) is filled with cooling water for cooling;
in the gas condenser: the cavity of the lower cavity (LNQ-XQ) is not filled with water, a gas space is reserved, the gas space is communicated with the atmosphere through a balance gas pipe (LNQ-QG2), and the opening position of the balance gas pipe (LNQ-QG2) in the atmosphere is higher than the highest point of water communicated with the upper cavity (LNQ-SQ);
the second separating valve (FLF2) of the gas condenser is also a water-gas separating valve (FLF) which only releases water and does not release gas, like the first separating valve (FLF1) of the mixing vessel (R3);
the upper end of a conical cavity (FLF-ZXQ) of a second separation valve (FLF2) of the gas condenser is communicated with the lower cavity (LNQ-XQ), the lower end of the conical cavity (FLF-ZXQ) of the second separation valve (FLF2) is higher than the bottom of the lower cavity (LNQ-XQ), and the lowest point of an outlet of a water outlet pipe (FLF-CSG) of a second separation valve (FLF2) is higher than the bottom of the lower cavity (LNQ-XQ);
the heat exchanger of the gas condenser is composed of a plurality of heat exchange tubes (LNQ-HG);
the heat exchange tube (LNQ-HG) of the gas condenser comprises a first tube (LNQ-HG-1), a second tube (LNQ-HG-2), a third tube (LNQ-HG-3), a fourth tube (LNQ-HG-4), a fifth tube (LNQ-HG-5), a sixth tube (LNQ-HG-6) and a seventh tube (LNQ-HG-7);
in the heat exchange tube (LNQ-HG) of the gas condenser: the first pipe (LNQ-HG-1) is arranged in a mode that the axis is horizontal;
in the heat exchange tube (LNQ-HG) of the gas condenser: the second pipe (LNQ-HG-1) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the third pipe (LNQ-HG-3) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the fourth pipe (LNQ-HG-4) is arranged in a mode that the axis is horizontal;
in the heat exchange tube (LNQ-HG) of the gas condenser: the fifth pipe (LNQ-HG-5) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the sixth pipe (LNQ-HG-6) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the seventh pipe (LNQ-HG-7) is arranged in a mode that the axis is horizontal;
in the heat exchange tube (LNQ-HG) of the gas condenser: the lower end of the second pipe (LNQ-HG-1) is open to the outside;
in the heat exchange tube (LNQ-HG) of the gas condenser: the lower end of the sixth pipe (LNQ-HG-6) has an opening to the outside;
in the heat exchange tube (LNQ-HG) of the gas condenser: the left end of the first pipe (LNQ-HG-1), the lower end of the third pipe (LNQ-HG-3) and the upper end of the second pipe (LNQ-HG-2) are connected and communicated;
in the heat exchange tube (LNQ-HG) of the gas condenser: the right end of the seventh pipe (LNQ-HG-7), the lower end of the fifth pipe (LNQ-HG-5) and the upper end of the sixth pipe (LNQ-HG-6) are connected and communicated;
in the heat exchange tube (LNQ-HG) of the gas condenser: the upper end of the third pipe (LNQ-HG-3) is connected and communicated with the right end of the fourth pipe (LNQ-HG-4);
in the heat exchange tube (LNQ-HG) of the gas condenser: the upper end of the fifth pipe (LNQ-HG-5) is connected and communicated with the left end of the fourth pipe (LNQ-HG-4);
the heat exchange tubes (LNQ-HG) of the gas condenser form a heat exchanger by a combination method that two adjacent heat exchange tubes (LNQ-HG) are named as a left heat exchange tube and a right heat exchange tube, and a first tube (LNQ-HG-1) of the left heat exchange tube is connected and communicated with a seventh tube (LNQ-HG-7) of the right heat exchange tube;
in the gas condenser: the horizontal positions of the openings of the lower ends of the second tubes (LNQ-HG-1) and the lower ends of the sixth tubes (LNQ-HG-6) of all the heat exchange tubes (LNQ-HG) of the heat exchanger are lower than the upper end of the conical cavity (FLF-ZXQ) of the second separation valve (FLF 2);
in the gas condenser: the openings of the lower ends of the second tubes (LNQ-HG-1) and the lower ends of the sixth tubes (LNQ-HG-6) of all heat exchange tubes (LNQ-HG) of the heat exchanger are in the lower chamber (LNQ-XQ);
in the gas condenser: opening of lower end of second tube (LNQ-HG-1) of all heat exchange tubes (LNQ-HG) of heat exchanger and sixth tube (LNQ-HG-6)
In the gas condenser: an air inlet of an exhaust pump (B2) is communicated with a seventh pipe (LNQ-HG-7) of the leftmost heat exchange pipe (LNQ-HG), an air outlet of the exhaust pump (B2) is communicated with an air inlet of an exhaust pipe (LNQ-PQG), an air inlet pipe (LNQ-JG) is communicated with a first pipe (LNQ-HG-1) of the rightmost heat exchange pipe (LNQ-HG), the gas passes through a heat exchanger and is cooled, water droplets contained in the gas are condensed into water drops, the water drops fall into a lower cavity (LNQ-XQ), and after the water in the lower cavity (LNQ-XQ) reaches a certain water level, a part of the water drops is discharged and retained through a second separation valve (FLF2) to remove the water component contained in the gas;
the mixing vessel (R3) is identical to the inlet pipe (LNQ-JG) of the gas condenser;
an upper cavity (LNQ-SQ) of the gas condenser is communicated with a second cavity of the refrigeration container (R1) through a first condensation exchange water pipe (SG1) and a second condensation exchange water pipe (SG2), and a circulating pump (SG2) is arranged on the second condensation exchange water pipe (SG2) to ensure that cooling water in the upper cavity (LNQ-SQ) of the gas condenser is circulated with cold water in the refrigeration container (R1);
an exhaust pump (B2) of the gas condenser is started, gas in an air inlet pipe (JQG) enters a refrigeration container (R1) to generate bubbles due to the action of negative pressure, the bubbles are contacted with cold water to reduce the temperature, part of gas dust in the gas falls into the cold water in the refrigeration container (R1), and after the bubbles burst, the cooled gas enters a mixing container (R3) through a first heat insulation pipe (GRG 1); the hot steam of the heating container (R2) enters the mixing container (R3) due to the negative pressure; the cooled gas is fully mixed with the hot steam due to the stirring of the stirrer (JBQ), the temperature of solid dust contained in the cooled gas is lower to form a raindrop core, the temperature of the hot steam is reduced when the hot steam contacts the raindrop core, the hot steam is condensed due to the action of the gas condenser to form larger raindrops, and the raindrops fall into the lower cavity of the gas condenser in the heat exchange tube (LNQ-HG) of the gas condenser and carry the solid dust back to the heating container (R2).
Example 3, fig. 6-13, a gas dusting system, characterized by: the device is composed of a mechanical rotary bubble generator (R1), a heating container (R2), a mixing container (R3), a gas condenser, an air inlet pipeline (JQG) and a refrigerating and heating device (3);
the mechanical rotary type bubble generator (R1) comprises a rotor (1), a container (2), a cover (3), a bearing (4), a motor (5) and a rivet (6);
the rotor (1) comprises a connecting part (1-1), a back-off container (1-2), a waist opening (1-3), an air outlet (1-4), an air inlet opening (1-8) and a driving blade group (1-5);
in a rotor (1): the connecting part (1-1) is cylindrical, a connecting hole (1-7) is formed in the connecting part (1-1), the axis of the connecting part (1-1) is vertically intersected with the axis of the connecting hole (1-7), and a motor connecting structure is arranged at the upper end of the connecting part (1-1);
in a rotor (1): the inverted container (1-2) is cylindrical, a cylindrical cavity (1-6) is arranged in the inverted container (1-2), the cylindrical cavity (1-6) is coaxial with the inverted container (1-2), and the upper end of the inverted container (1-2) is closed;
in a rotor (1): the waist opening (1-3) is frustum-shaped, the waist opening (1-3) is provided with a frustum-shaped cavity, the axis of the frustum-shaped cavity of the waist opening (1-3) is superposed with the axis of the waist opening (1-3), and the large opening end of the frustum-shaped cavity of the waist opening (1-3) is communicated with the lower end of the inverted container (1-2);
in a rotor (1): the air inlet openings (1-8) are cylindrical, the air inlet openings (1-8) are provided with cylindrical cavities, the axes of the air inlet openings (1-8) are coaxial with the cylindrical cavities of the air inlet openings (1-8), and the cylindrical cavities of the air inlet openings (1-8) are communicated with the small opening ends of the frustum-shaped cavities of the waist openings (1-3);
in a rotor (1): the driving blade group (1-5) is composed of an upper blade (1-5-3-1) and a lower blade (1-5-3-2), and both the upper blade and the lower blade are arc-shaped; the upper blade (1-5-3-1) is parallel to the lower blade (1-5-3-2), the inner side of the upper blade (1-5-3-1) is connected with the outer wall of the inverted container (1-2), the inner side of the lower blade (1-5-3-2) is connected with the outer wall of the inverted container (1-2), the space between the outer side of the upper blade (1-5-3-1) and the outer side of the lower blade (1-5-3-2) is open, and the distance from the head end of the upper blade (1-5-3-1) to the upper end of the inverted container (1-2) is greater than the distance from the tail end of the upper blade (1-5-3-1) to the upper end of the inverted container (1-2); the distance from the head end of the lower blade (1-5-3-2) to the upper end of the inverted container (1-2) is greater than the distance from the tail end of the lower blade (1-5-3-2) to the upper end of the inverted container (1-2); the outer edge arc line of the lower blade (1-5-3-2) is coplanar with the outer edge arc line of the upper blade (1-5-3-1); the length of the outer edge arc line of the upper blade (1-5-3-1) is one sixth of the circle where the foreign arc line is located; the number of the driving blade groups (1-5) is 3(1-5-1, 1-5-2, 1-5-3), and the 3 driving blade groups (1-5-1, 1-5-2, 1-5-3) are distributed in a circumferential array by taking the axis of the inverted container (1-2) as a central line;
in a rotor (1): the air outlet (1-4) penetrates through the wall of the inverted container (1-2), and the inner end of the air outlet (1-4) is communicated with the cylindrical cavity (1-6) of the inverted container (1-2); the outer end space positions of the air outlet holes (1-4) are positioned between the tail ends of the upper blades (1-5-3-1) of the driving blade groups (1-5) and the tail ends of the lower blades (1-5-3-2) of the driving blade groups (1-5), the number of the air outlet holes (1-4) is 3, each driving blade group (1-5) corresponds to one air outlet hole (1-4), and the 3 air outlet holes (1-4) are distributed in a circumferential array by taking the axis of the inverted container (1-2) as a central line; the container (2) comprises a containing cavity, a wave making cylinder (2-1), an air inlet pipe (2-2), a water permeable channel (2-3), a supporting part (2-4) and container feet (2-5); in the container (2): the cavity is a frustum-shaped cavity, the large end of the cavity faces upwards, and the lower end of the cavity faces downwards;
in the container (2): the wave making cylinder (2-1) is positioned in the containing cavity, the wave making cylinder (2-1) is cylindrical, the inner wall of the wave making cylinder (2-1) is provided with 3 concave cambered surfaces (2-1-1), the 3 concave cambered surfaces (2-1-1) are distributed in a circumferential array by taking the axis of the wave making cylinder (2-1) as a central line, and the distance from the surface of the concave cambered surface (2-1-1) to the axis of the wave making cylinder (2-1) is greater than the distance from the part without the concave cambered surface (2-1-1) on the inner wall of the wave making cylinder (2-1) to the axis of the wave making cylinder (2-1); the span of the first end and the second end of the concave cambered surface (2-1-1) in the inner section circle of the wave making cylinder (2-1) is one sixth of the inner section circle of the wave making cylinder (2-1); the first end of the supporting part (2-4) is connected with the outer wall of the wave making cylinder (2-1), and the second end of the supporting part (2-4) is connected with the side surface of the containing cavity to play a role in supporting the wave making cylinder (2-1); the wave making cylinder (2-1) is coaxial with the containing cavity, and the horizontal height of the upper end of the wave making cylinder (2-1) is lower than that of the large end of the containing cavity;
in the container (2): the water permeable channel (2-3) is positioned between the lower end of the wave making cylinder (2-1) and the bottom of the containing cavity, and water in the containing cavity can enter the wave making cylinder (2-1) through the water permeable channel (2-3);
in the container (2): the air inlet pipe (2-2) is coaxial with the wave making cylinder (2-1), and the air inlet pipe (2-2) penetrates through the bottom interface of the cavity from the outside and enters the wave making cylinder (2-1);
in the container (2): the container feet (2-5) are positioned at the lower part of the container, play a role in supporting and are convenient to place;
the cover (3) comprises a body, a motor supporting part (3-1), a motor shaft hole (3-2), an air outlet pipe (3-3) and a motor shaft waterproof column (3-4);
in the lid (3): the body is disc-shaped, and the motor supporting part (3-1) is cylindrical and is used for supporting the motor;
in the lid (3): the motor supporting part (3-1) is positioned above the body, the motor supporting part (3-1) is coaxial with the body, and the outer diameter of the motor supporting part (3-1) is smaller than that of the body;
in the lid (3): the motor shaft waterproof column (3-4) is positioned below the body, and the motor shaft waterproof column (3-4) is coaxial with the body;
in the lid (3): the inner diameter of the motor shaft hole (3-2) is smaller than the outer diameter of the motor supporting part (3-1); the motor shaft hole (3-2) is coaxial with the motor shaft waterproof column (3-4), the first end of the motor shaft hole (3-2) is communicated with the motor supporting part (3-1), and the second end of the motor shaft hole (3-2) is positioned on the lower surface of the motor shaft waterproof column (3-4);
in the lid (3): the air outlet pipe (3-3) is positioned above the body, and the pipe cavity of the air outlet pipe (3-3) penetrates through the body; the opening of the tube cavity of the air outlet tube (3-3) is positioned on the lower surface of the body;
the bearing (4) is used for connecting the connecting part (1-1) of the rotor (1) and the cover; the motor (5) is arranged on a motor supporting part (3-1) of the cover (3), the connecting part of the rotor (1) penetrates through the cover (3) to be connected with a motor shaft hole (3-2), and the cover (3) is arranged at the upper end of the container (2); an air inlet pipe (2-2) of the container (2) extends into a cylindrical cavity (1-6) of the inverted container (1-2) of the rotor (1);
the rotor (1) is coaxial with the wave making cylinder (2-1) of the inverted container (1-2);
the driving blade group (1-5) of the rotor (1) is positioned inside the wave making cylinder (2-1) of the inverted container (1-2), and the distance between the outer edge arc line of the lower blade (1-5-3-2) of the driving blade group (1-5) of the rotor (1) and the place, without the concave arc surface (2-1-1), of the wave making cylinder (2-1) of the container (2) is smaller than the thickness of the lower blade (1-5-3-2); the motor (5) is used for driving the rotor (1) to rotate at a constant speed.
The mechanical rotary bubble generator (R1) is partially filled with cold water, and the height of the cold water surface of the mechanical rotary bubble generator (R1) is higher than the top end of the wave making cylinder (2-1);
the interior of the heating container (R2) is filled with hot water;
the mixing container (R3) is internally provided with a stirrer (JBQ), and the stirrer (JBQ) is driven by a motor;
a first separation valve (FLF1) is arranged in the mixing container (R3);
a first separating valve (FLF1) of the mixing container (R3) is positioned at the bottom of the mixing container (R3) and is used for discharging water at the bottom of the mixing container (R3); the second separating valve (FLF2) of the mixing vessel (R3) is a water-gas separating valve (FLF) releasing only water and not gas;
the water-gas separation valve (FLF) comprises a water outlet pipe (FLF-CSG), a conical cavity (FLF-ZXQ), a heavy ball (FLF-ZQ) and a floating ball (FLF-FQ); in the second separation valve (FLF2) of the mixing vessel (R3): the conical cavity (FLF-ZXQ) is arranged in an axis-vertical mode, the large end of the conical cavity (FLF-ZXQ) is arranged above, and the small end of the conical cavity (FLF-ZXQ) is arranged below;
in the second separation valve (FLF2) of the mixing vessel (R3): the density of the heavy ball (FLF-ZQ) is larger than that of water in the application environment;
in the second separation valve (FLF2) of the mixing vessel (R3): the density of the floating ball (FLF-FQ) is less than that of water in an application environment;
in the second separation valve (FLF2) of the mixing vessel (R3): the lower end of the conical cavity (FLF-ZXQ) is connected with the highest point of the water outlet pipe (FLF-CSG);
in the second separation valve (FLF2) of the mixing vessel (R3): the diameter of the heavy ball (FLF-ZQ) is smaller than the large end of the conical cavity (FLF-ZXQ), and the diameter of the heavy ball (FLF-ZQ) is larger than the small end of the conical cavity (FLF-ZXQ);
in the second separation valve (FLF2) of the mixing vessel (R3): a heavy ball (FLF-ZQ) device is arranged in the conical cavity (FLF-ZXQ);
in the second separation valve (FLF2) of the mixing vessel (R3): the floating ball (FLF-FQ) is connected with the heavy ball (FLF-ZQ) through a flexible wire, when the floating ball (FLF-FQ) is floated by water in the cavity of the water-gas separation valve (FLF), the heavy ball (FLF-ZQ) is pulled up by the floating ball (FLF-FQ), the lower end of the conical cavity (FLF-ZXQ) is released, the water is discharged through the upper end of the conical cavity (FLF-ZXQ), the lower end of the conical cavity (FLF-ZXQ) and the water outlet pipe (FLF-CSG), when the water level lowers the heavy ball (FLF-ZQ) and falls on the lower end of the conical cavity (FLF-ZXQ) because of gravity, the lower end of the conical cavity (FLF-ZXQ) is closed and does not discharge water any more, since the floating ball (FLF-FQ) is connected with the heavy ball (FLF-ZQ) through a flexible wire, when the water surface descends to the height of the heavy ball and the line is lengthened, the lower end of the conical cavity (FLF-ZXQ) is closed, so that the gas cannot be discharged;
the upper end of a conical cavity (FLF-ZXQ) of a second separation valve (FLF2) of the mixing container (R3) is communicated with the lower cavity (LNQ-XQ), the lower end of the conical cavity (FLF-ZXQ) of the second separation valve (FLF2) is higher than the bottom of the lower cavity (LNQ-XQ), and the lowest point of an outlet of a water outlet pipe (FLF-CSG) of the second separation valve (FLF2) is higher than the bottom of the lower cavity (LNQ-XQ);
the refrigerating and heating device (3) is provided with a heating end and a refrigerating end, the refrigerating end of the refrigerating and heating device (3) is connected with the mechanical rotary bubble generator (R1) and used for cooling cold water in the mechanical rotary bubble generator (R1), and the heating end of the refrigerating and heating device (3) is connected with the heating container (R2) and used for heating hot water in the heating container (R2);
the top of the mechanical rotary bubble generator (R1) is communicated with the top of the mixing container (R3) through a first heat insulation pipe (GRG1), a first check valve (DXF1) is arranged on the pipeline of the first heat insulation pipe (GRG1), and the gas in the mixing container (R3) cannot flow back to the mechanical rotary bubble generator (R1);
the side wall above the water surface on the left side of the heating container (R2) is communicated with the wall on the right side of the mixing container (R3) through a second heat insulation pipe (GRG 2);
the water outlet pipe of the first separating valve (FLF1) of the heating container (R2) is communicated with the part below the water surface of the heating container (R2) through a third heat-insulating pipe (GRG 3);
the gas condenser comprises an upper cavity (LNQ-SQ), a lower cavity (LNQ-XQ), an air inlet pipe (LNQ-JG), an air outlet pipe (LNQ-PQG), a heat exchanger, a balance air pipe (LNQ-QG2), a second separation valve (FLF2), a water outlet pipe (LNQ-PSG) and an air exhaust pump (B2);
in the gas condenser: the upper chamber (LNQ-SQ) is filled with cooling water for cooling;
in the gas condenser: the cavity of the lower cavity (LNQ-XQ) is not filled with water, a gas space is reserved, the gas space is communicated with the atmosphere through a balance gas pipe (LNQ-QG2), and the opening position of the balance gas pipe (LNQ-QG2) in the atmosphere is higher than the highest point of water communicated with the upper cavity (LNQ-SQ);
the second separation valve (FLF2) of the gas condenser is a water-gas separation valve (FLF) which only releases water and does not release gas;
the water-gas separation valve (FLF) comprises a water outlet pipe (FLF-CSG), a conical cavity (FLF-ZXQ), a heavy ball (FLF-ZQ) and a floating ball (FLF-FQ);
in the second separation valve (FLF2) of the gas condenser: the conical cavity (FLF-ZXQ) is arranged in an axis-vertical mode, the large end of the conical cavity (FLF-ZXQ) is arranged above, and the small end of the conical cavity (FLF-ZXQ) is arranged below;
in the second separation valve (FLF2) of the gas condenser: the density of the heavy ball (FLF-ZQ) is larger than that of water in the application environment;
in the second separation valve (FLF2) of the gas condenser: the density of the floating ball (FLF-FQ) is less than that of water in an application environment;
in the second separation valve (FLF2) of the gas condenser: the lower end of the conical cavity (FLF-ZXQ) is connected with the highest point of the water outlet pipe (FLF-CSG); in the second separation valve (FLF2) of the gas condenser: the diameter of the heavy ball (FLF-ZQ) is smaller than the large end of the conical cavity (FLF-ZXQ), and the diameter of the heavy ball (FLF-ZQ) is larger than the small end of the conical cavity (FLF-ZXQ);
in the second separation valve (FLF2) of the gas condenser: a heavy ball (FLF-ZQ) device is arranged in the conical cavity (FLF-ZXQ);
in the second separation valve (FLF2) of the gas condenser: the floating ball (FLF-FQ) is connected with the heavy ball (FLF-ZQ) through a flexible wire, when the floating ball (FLF-FQ) is floated by water in the cavity of the water-gas separation valve (FLF), the heavy ball (FLF-ZQ) is pulled up by the floating ball (FLF-FQ), the lower end of the conical cavity (FLF-ZXQ) is released, the water is discharged through the upper end of the conical cavity (FLF-ZXQ), the lower end of the conical cavity (FLF-ZXQ) and the water outlet pipe (FLF-CSG), when the water level lowers the heavy ball (FLF-ZQ) and falls on the lower end of the conical cavity (FLF-ZXQ) because of gravity, the lower end of the conical cavity (FLF-ZXQ) is closed and does not discharge water any more, since the floating ball (FLF-FQ) is connected with the heavy ball (FLF-ZQ) through a flexible wire, when the water surface descends to the height of the heavy ball and the line is lengthened, the lower end of the conical cavity (FLF-ZXQ) is closed, so that the gas cannot be discharged;
the upper end of a conical cavity (FLF-ZXQ) of a second separation valve (FLF2) of the gas condenser is communicated with the lower cavity (LNQ-XQ), the lower end of the conical cavity (FLF-ZXQ) of the second separation valve (FLF2) is higher than the bottom of the lower cavity (LNQ-XQ), and the lowest point of an outlet of a water outlet pipe (FLF-CSG) of a second separation valve (FLF2) is higher than the bottom of the lower cavity (LNQ-XQ);
the heat exchanger of the gas condenser is composed of a plurality of heat exchange tubes (LNQ-HG);
the heat exchange tube (LNQ-HG) of the gas condenser comprises a first tube (LNQ-HG-1), a second tube (LNQ-HG-2), a third tube (LNQ-HG-3), a fourth tube (LNQ-HG-4), a fifth tube (LNQ-HG-5), a sixth tube (LNQ-HG-6) and a seventh tube (LNQ-HG-7); in the heat exchange tube (LNQ-HG) of the gas condenser: the first pipe (LNQ-HG-1) is arranged in a mode that the axis is horizontal;
in the heat exchange tube (LNQ-HG) of the gas condenser: the second pipe (LNQ-HG-1) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the third pipe (LNQ-HG-3) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the fourth pipe (LNQ-HG-4) is arranged in a mode that the axis is horizontal;
in the heat exchange tube (LNQ-HG) of the gas condenser: the fifth pipe (LNQ-HG-5) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the sixth pipe (LNQ-HG-6) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the seventh pipe (LNQ-HG-7) is arranged in a mode that the axis is horizontal;
in the heat exchange tube (LNQ-HG) of the gas condenser: the lower end of the second pipe (LNQ-HG-1) is open to the outside;
in the heat exchange tube (LNQ-HG) of the gas condenser: the lower end of the sixth pipe (LNQ-HG-6) has an opening to the outside;
in the heat exchange tube (LNQ-HG) of the gas condenser: the left end of the first pipe (LNQ-HG-1), the lower end of the third pipe (LNQ-HG-3) and the upper end of the second pipe (LNQ-HG-2) are connected and communicated;
in the heat exchange tube (LNQ-HG) of the gas condenser: the right end of the seventh pipe (LNQ-HG-7), the lower end of the fifth pipe (LNQ-HG-5) and the upper end of the sixth pipe (LNQ-HG-6) are connected and communicated;
in the heat exchange tube (LNQ-HG) of the gas condenser: the upper end of the third pipe (LNQ-HG-3) is connected and communicated with the right end of the fourth pipe (LNQ-HG-4);
in the heat exchange tube (LNQ-HG) of the gas condenser: the upper end of the fifth pipe (LNQ-HG-5) is connected and communicated with the left end of the fourth pipe (LNQ-HG-4);
the heat exchange tubes (LNQ-HG) of the gas condenser are combined by naming two adjacent heat exchange tubes (LNQ-HG) as a left heat exchange tube and a right heat exchange tube, and then a first tube (LNQ-HG-1) of the left heat exchange tube is connected and communicated with a seventh tube (LNQ-HG-7) of the right heat exchange tube;
in the gas condenser: the horizontal positions of the openings of the lower ends of the second tubes (LNQ-HG-1) and the lower ends of the sixth tubes (LNQ-HG-6) of all the heat exchange tubes (LNQ-HG) of the heat exchanger are lower than the upper end of the conical cavity (FLF-ZXQ) of the second separation valve (FLF 2);
in the gas condenser: the openings of the lower ends of the second tubes (LNQ-HG-1) and the lower ends of the sixth tubes (LNQ-HG-6) of all heat exchange tubes (LNQ-HG) of the heat exchanger are in the lower chamber (LNQ-XQ);
in the gas condenser: opening of lower end of second tube (LNQ-HG-1) of all heat exchange tubes (LNQ-HG) of heat exchanger and sixth tube (LNQ-HG-6)
In the gas condenser: an air inlet of an exhaust pump (B2) is communicated with a seventh pipe (LNQ-HG-7) of the leftmost heat exchange pipe (LNQ-HG), an air outlet of the exhaust pump (B2) is communicated with an air inlet of an exhaust pipe (LNQ-PQG), an air inlet pipe (LNQ-JG) is communicated with a first pipe (LNQ-HG-1) of the rightmost heat exchange pipe (LNQ-HG), the gas passes through a heat exchanger and is cooled, water droplets contained in the gas are condensed into water drops, the water drops fall into a lower cavity (LNQ-XQ), and after the water in the lower cavity (LNQ-XQ) reaches a certain water level, a part of the water drops is discharged and retained through a second separation valve (FLF2) to remove the water component contained in the gas;
the mixing container (R3) is communicated with an air inlet pipe (LNQ-JG) of the gas condenser;
the upper cavity (LNQ-SQ) of the gas condenser is communicated with the mechanical rotary bubble generator (R1) through a first condensation exchange water pipe (SG1) and a second condensation exchange water pipe (SG2), and a circulating pump (SG2) is arranged on the second condensation exchange water pipe (SG2) to ensure that cooling water in the upper cavity (LNQ-SQ) of the gas condenser is circulated with cold water in the mechanical rotary bubble generator (R1);
an exhaust pump (B2) of the gas condenser is started, gas in an air inlet pipe (JQG) enters a mechanical rotary type bubble generator (R1) to generate bubbles due to the action of negative pressure, the bubbles are contacted with cold water to reduce the temperature, part of gas dust in the gas falls into the cold water of the mechanical rotary type bubble generator (R1), and after the bubbles are burst, the cooled gas enters a mixing container (R3) through a first heat insulation pipe (GRG 1); the hot steam of the heating container (R2) enters the mixing container (R3) due to the negative pressure; the cooled gas is fully mixed with the hot steam due to the stirring of the stirrer (JBQ), the temperature of solid dust contained in the cooled gas is lower to form a raindrop core, the temperature of the hot steam is reduced when the hot steam contacts the raindrop core, the hot steam is condensed due to the action of the gas condenser to form larger raindrops, and the raindrops fall into a lower cavity of the gas condenser in a heat exchange tube (LNQ-HG) of the gas condenser and carry the solid dust back to the heating container (R2); the horizontal position of the opening of the first condensation exchange water pipe (SG1) in the mechanical rotary type bubble generator (R1) is lower than the top end of the wave making cylinder (2-1) of the mechanical rotary type bubble generator (R1), and the horizontal position of the opening of the first condensation exchange water pipe (SG1) in the mechanical rotary type bubble generator (R1) is higher than the bottom end of the wave making cylinder (2-1) of the mechanical rotary type bubble generator (R1); the horizontal position of the opening of the second condensation exchange water pipe (SG2) in the mechanical rotary type bubble generator (R1) is lower than the top end of the wave making cylinder (2-1) of the mechanical rotary type bubble generator (R1), and the horizontal position of the opening of the second condensation exchange water pipe (SG2) in the mechanical rotary type bubble generator (R1) is higher than the bottom end of the wave making cylinder (2-1) of the mechanical rotary type bubble generator (R1).
Example 4, modification of the protocol based on example 2 or 3: further: the bottom of the heating container (R2) is provided with a sewage discharge valve for discharging sewage.
Example 5, modification of the protocol based on example 2 or 3: further: the refrigeration container (R1) is a metal container.
Example 6, modification of the protocol based on example 2 or 3: further: the heating container (R2) is a metal container.
Example 7, modification of the protocol based on example 2 or 3: further: the mixing vessel (R3) is a metal vessel.
Example 8, modification of the protocol based on example 2 or 3: further: the main element of the refrigerating and heating device (ZLQ-3) is a semiconductor refrigerating sheet which is also called a Peltier.
Example 9, modification of the protocol based on example 2 or 3: further: the main element of the refrigerating and heating device (ZLQ-3) is a vortex refrigerator, also called a vortex tube or a cold air device or a vortex cooler.
When the rotor of the mechanical rotary bubble generator (R1) rotates, water flow is formed between the upper blade (1-5-3-1) and the lower blade (1-5-3-2) by the driving blade group (1-5) to impact the air outlet (1-4) of the rotor (1), and the pressure of the liquid driving channel of the driving blade group (1-5) is periodically changed due to the fact that the surface of the wave making cylinder (2-1) of the container (2) is provided with the concave cambered surface (2-1-1), so that the water flow driven by the driving blade group (1-5) is periodically fluctuated, air bands are not easily generated near the air holes, and efficiency is improved; the service life of the motor can be prolonged without changing the speed of the rotor, so that the service life of the whole device can be prolonged; because no solid structure impacts the bubbles, the local temperature is reduced; the mechanical rotary bubble generator (R1) has a high lifetime because there is no solid structure to impact the bubbles and no bubble bursting impact erodes the solid structure. The mechanical rotary bubble generator (R1) has the advantages of long service life, low energy consumption and simple structure, and is beneficial to reducing local temperature.
The mechanical rotary bubble generator (R1) creates a new idea.

Claims (8)

1. The gas condenser comprises an upper cavity (LNQ-SQ), a lower cavity (LNQ-XQ), a condenser air inlet pipe (LNQ-JG), an air outlet pipe (LNQ-PQG), a heat exchanger, a balance air pipe (LNQ-QG2), a second separation valve (FLF2), a water outlet pipe (LNQ-PSG) and an exhaust pump (B2);
in the gas condenser: the upper chamber (LNQ-SQ) is filled with cooling water for cooling;
in the gas condenser: the cavity of the lower cavity (LNQ-XQ) is not filled with water, a gas space is reserved, the gas space is communicated with the atmosphere through a balance gas pipe (LNQ-QG2), and the opening position of the balance gas pipe (LNQ-QG2) in the atmosphere is higher than the highest point of water communicated with the upper cavity (LNQ-SQ);
the second separation valve (FLF2) of the gas condenser is a water-gas separation valve (FLF) which only releases water and does not release gas;
the water-gas separation valve (FLF) comprises a water outlet pipe (FLF-CSG), a conical cavity (FLF-ZXQ), a heavy ball (FLF-ZQ) and a floating ball (FLF-FQ);
in the second separation valve (FLF2) of the gas condenser: the conical cavity (FLF-ZXQ) is arranged in an axis-vertical mode, the large end of the conical cavity (FLF-ZXQ) is arranged above, and the small end of the conical cavity (FLF-ZXQ) is arranged below;
in the second separation valve (FLF2) of the gas condenser: the density of the heavy ball (FLF-ZQ) is larger than that of water in the application environment;
in the second separation valve (FLF2) of the gas condenser: the density of the floating ball (FLF-FQ) is less than that of water in an application environment;
in the second separation valve (FLF2) of the gas condenser: the lower end of the conical cavity (FLF-ZXQ) is connected with the highest point of the water outlet pipe (FLF-CSG);
in the second separation valve (FLF2) of the gas condenser: the diameter of the heavy ball (FLF-ZQ) is smaller than the large end of the conical cavity (FLF-ZXQ), and the diameter of the heavy ball (FLF-ZQ) is larger than the small end of the conical cavity (FLF-ZXQ);
in the second separation valve (FLF2) of the gas condenser: a heavy ball (FLF-ZQ) device is arranged in the conical cavity (FLF-ZXQ);
in the second separation valve (FLF2) of the gas condenser: the floating ball (FLF-FQ) is connected with the heavy ball (FLF-ZQ) through a flexible wire, when the floating ball (FLF-FQ) is floated by water in the cavity of the water-gas separation valve (FLF), the heavy ball (FLF-ZQ) is pulled up by the floating ball (FLF-FQ), the lower end of the conical cavity (FLF-ZXQ) is released, the water is discharged through the upper end of the conical cavity (FLF-ZXQ), the lower end of the conical cavity (FLF-ZXQ) and the water outlet pipe (FLF-CSG), when the water level lowers the heavy ball (FLF-ZQ) and falls on the lower end of the conical cavity (FLF-ZXQ) because of gravity, the lower end of the conical cavity (FLF-ZXQ) is closed and does not discharge water any more, since the floating ball (FLF-FQ) is connected with the heavy ball (FLF-ZQ) through a flexible wire, when the water surface descends to the height of the heavy ball and the line is lengthened, the lower end of the conical cavity (FLF-ZXQ) is closed, so that the gas cannot be discharged;
the upper end of a conical cavity (FLF-ZXQ) of a second separation valve (FLF2) of the gas condenser is communicated with the lower cavity (LNQ-XQ), the lower end of the conical cavity (FLF-ZXQ) of the second separation valve (FLF2) is higher than the bottom of the lower cavity (LNQ-XQ), and the lowest point of an outlet of a water outlet pipe (FLF-CSG) of a second separation valve (FLF2) is higher than the bottom of the lower cavity (LNQ-XQ);
the heat exchanger of the gas condenser is composed of a plurality of heat exchange tubes (LNQ-HG);
the heat exchange tube (LNQ-HG) of the gas condenser comprises a first tube (LNQ-HG-1), a second tube (LNQ-HG-2), a third tube (LNQ-HG-3), a fourth tube (LNQ-HG-4), a fifth tube (LNQ-HG-5), a sixth tube (LNQ-HG-6) and a seventh tube (LNQ-HG-7);
in the heat exchange tube (LNQ-HG) of the gas condenser: the first pipe (LNQ-HG-1) is arranged in a mode that the axis is horizontal;
in the heat exchange tube (LNQ-HG) of the gas condenser: a second tube (LNQ-HG-2)) lying in an axis-vertical manner;
in the heat exchange tube (LNQ-HG) of the gas condenser: the third pipe (LNQ-HG-3) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the fourth pipe (LNQ-HG-4) is arranged in a mode that the axis is horizontal;
in the heat exchange tube (LNQ-HG) of the gas condenser: the fifth pipe (LNQ-HG-5) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the sixth pipe (LNQ-HG-6) is arranged in an axis vertical mode;
in the heat exchange tube (LNQ-HG) of the gas condenser: the seventh pipe (LNQ-HG-7) is arranged in a mode that the axis is horizontal;
in the heat exchange tube (LNQ-HG) of the gas condenser: a second tube (LNQ-HG-2)) having a lower end open to the outside;
in the heat exchange tube (LNQ-HG) of the gas condenser: the lower end of the sixth pipe (LNQ-HG-6) has an opening to the outside;
in the heat exchange tube (LNQ-HG) of the gas condenser: the left end of the first pipe (LNQ-HG-1), the lower end of the third pipe (LNQ-HG-3) and the upper end of the second pipe (LNQ-HG-2) are connected and communicated;
in the heat exchange tube (LNQ-HG) of the gas condenser: the right end of the seventh pipe (LNQ-HG-7), the lower end of the fifth pipe (LNQ-HG-5) and the upper end of the sixth pipe (LNQ-HG-6) are connected and communicated;
in the heat exchange tube (LNQ-HG) of the gas condenser: the upper end of the third pipe (LNQ-HG-3) is connected and communicated with the right end of the fourth pipe (LNQ-HG-4);
in the heat exchange tube (LNQ-HG) of the gas condenser: the upper end of the fifth pipe (LNQ-HG-5) is connected and communicated with the left end of the fourth pipe (LNQ-HG-4);
the heat exchange tubes (LNQ-HG) of the gas condenser form a heat exchanger by a combination method that two adjacent heat exchange tubes (LNQ-HG) are named as a left heat exchange tube and a right heat exchange tube, and a first tube (LNQ-HG-1) of the left heat exchange tube is connected and communicated with a seventh tube (LNQ-HG-7) of the right heat exchange tube;
in the gas condenser: the horizontal positions of the openings of the lower ends of the second tubes (LNQ-HG-2)) and the openings of the lower ends of the sixth tubes (LNQ-HG-6) of all the heat exchange tubes (LNQ-HG) of the heat exchanger are lower than the upper end of the conical chamber (FLF-ZXQ) of the second separation valve (FLF 2);
in the gas condenser: the openings of the lower ends of the second tubes (LNQ-HG-2)) and the lower ends of the sixth tubes (LNQ-HG-6) of all heat exchange tubes (LNQ-HG) of the heat exchanger are in the lower chamber (LNQ-XQ);
in the gas condenser: an opening at the lower end of the second tube (LNQ-HG-2)) of all heat exchange tubes (LNQ-HG) of the heat exchanger and a sixth tube (LNQ-HG-6)
In the gas condenser: an air inlet of an exhaust pump (B2) is communicated with a seventh pipe (LNQ-HG-7) of the leftmost heat exchange pipe (LNQ-HG), an air outlet of the exhaust pump (B2) is communicated with an air inlet of an exhaust pipe (LNQ-PQG), an air inlet pipe (LNQ-JG) of a condenser is communicated with a first pipe (LNQ-HG-1) of the rightmost heat exchange pipe (LNQ-HG), the gas passes through a heat exchanger and is cooled, water droplets contained in the gas are condensed into water drops, the water drops fall into a lower cavity (LNQ-XQ), and after the water in the lower cavity (LNQ-XQ) reaches a certain water level, a part of the water drops are discharged and retained through a second separation valve (FLF2) to remove the water components contained in the gas;
the upper cavity (LNQ-SQ) is a square cavity.
2. A gas condenser as claimed in claim 1, wherein: the upper chamber (LNQ-SQ) has a temperature sensor therein.
3. A gas condenser as claimed in claim 1, wherein: the lower cavity (LNQ-XQ) has a temperature sensor therein.
4. A gas condenser as claimed in claim 1, wherein: the exhaust pipes (LNQ-PQG) are made of metal.
5. A gas condenser as claimed in claim 1, wherein: the exhaust pipes (LNQ-PQG) are made of plastic.
6. A gas condenser as claimed in claim 1, wherein: the material of the balance air pipe (LNQ-QG2) is plastic.
7. A gas condenser as claimed in claim 1, wherein: the balance air pipe (LNQ-QG2) is made of metal.
8. Environmental protection air dust collector, its characterized in that: having a gas condenser as claimed in claim 1.
CN201910095380.4A 2019-01-31 2019-01-31 Gas condenser and environment-friendly air dust removal device Active CN109647093B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910095380.4A CN109647093B (en) 2019-01-31 2019-01-31 Gas condenser and environment-friendly air dust removal device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910095380.4A CN109647093B (en) 2019-01-31 2019-01-31 Gas condenser and environment-friendly air dust removal device

Publications (2)

Publication Number Publication Date
CN109647093A CN109647093A (en) 2019-04-19
CN109647093B true CN109647093B (en) 2021-04-13

Family

ID=66122627

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910095380.4A Active CN109647093B (en) 2019-01-31 2019-01-31 Gas condenser and environment-friendly air dust removal device

Country Status (1)

Country Link
CN (1) CN109647093B (en)

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU1366841A1 (en) * 1986-05-26 1988-01-15 Московский Инженерно-Строительный Институт Им.В.В.Куйбышева System of technical water supply of steam turbine
JP2000304464A (en) * 1999-04-15 2000-11-02 Toshiba Corp Condenser
KR100858991B1 (en) * 2004-09-30 2008-09-18 마에카와 매뉴팩쳐링 캄파니 리미티드 Ammonia/CO2 Refrigeration System
CN103376849A (en) * 2012-04-27 2013-10-30 鸿富锦精密工业（深圳）有限公司 Container data center
CN103776282B (en) * 2014-02-20 2015-08-05 丹佛斯微通道换热器（嘉兴）有限公司 Heat exchanger
RU2581378C1 (en) * 2015-02-27 2016-04-20 Татьяна Дмитриевна Ходакова Hodakova horizontal adsorber
CN205607185U (en) * 2016-04-15 2016-09-28 德阳市中嘉实业股份有限公司 Heat exchanger convenient to dismantle heat exchange tube
CN105854486B (en) * 2016-05-27 2018-06-05 同济大学 A kind of afterheat recovery type sizing machine waste gas processing unit
CN106482323A (en) * 2016-12-09 2017-03-08 广东高而美制冷设备有限公司 A kind of double-tube heat exchanger and air-conditioning
CN207395509U (en) * 2017-10-09 2018-05-22 重庆新高机电有限公司 A kind of condenser
CN207797783U (en) * 2018-01-31 2018-08-31 四川普思瑞新材料有限公司 A kind of distribution condenser
CN109745800B (en) * 2019-01-25 2021-06-18 江苏师范大学 Gas dust removal system
CN109813168B (en) * 2019-01-25 2020-08-04 江苏师范大学 Heat exchange pipe and environment-friendly gas purification device
CN109603363B (en) * 2019-01-25 2021-06-15 江苏师范大学 Environment-friendly air dust removal system
CN109647095B (en) * 2019-01-25 2021-07-27 江苏师范大学 Heat exchange pipe for environment-friendly gas purification device
CN109939515B (en) * 2019-01-25 2021-06-18 江苏师范大学 Mechanical rotation type bubble generator and environment-friendly gas dust removal device
CN109621597B (en) * 2019-01-25 2021-06-15 江苏师范大学 Air dust removal purification system
CN109821327B (en) * 2019-01-25 2021-03-30 江苏师范大学 Environment-friendly gas dust removal device
CN109675384B (en) * 2019-01-25 2021-06-15 江苏师范大学 Environment protection device

Also Published As

Publication number Publication date
CN109647093A (en) 2019-04-19

Similar Documents

Publication Publication Date Title
CN109621597B (en) Air dust removal purification system
CN109939515B (en) Mechanical rotation type bubble generator and environment-friendly gas dust removal device
CN109603363B (en) Environment-friendly air dust removal system
CN109821327B (en) Environment-friendly gas dust removal device
CN109675384B (en) Environment protection device
CN109745800B (en) Gas dust removal system
CN109647095B (en) Heat exchange pipe for environment-friendly gas purification device
CN109813168B (en) Heat exchange pipe and environment-friendly gas purification device
CN102786167A (en) Laboratory wastewater treating device
CN109647093B (en) Gas condenser and environment-friendly air dust removal device
CN112807972B (en) High-efficient compound dust removal SOx/NOx control equipment of industrial waste gas
CN219023295U (en) Novel household energy-saving steam-water separator
CN208933026U (en) DAF air dissolved pump air bearing for sewage treatment
CN207324294U (en) A kind of externally positioned type demister
CN201001995Y (en) Landfill gas dewatering dust-cleaning device
CN1333076A (en) Bubble type air purifying method and purifier thereof
CN209771401U (en) Condensation dust removal defogging device for desulfurizing tower
CN209771800U (en) Desulfurization dust collector with whirl mixes
CN210448716U (en) High-efficiency pneumatic emulsification dust removal and desulfurization device for flue gas
CN213725686U (en) Water storage tank for compressed air dryer
CN204211510U (en) A kind of vertical three swirler air-floating apparatus
CN1713950A (en) Device for simultaneously cooling and removing liquid from a gas from a compressor
CN107321047B (en) A kind of multi-function vacuum filter for oil
CN106984116B (en) High-efficient gas purification tower and gas treatment system
CN210729107U (en) Industrial waste gas desulfurization treatment equipment

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant