CN209978057U - Waste gas and waste liquid treatment and heat recovery device - Google Patents
Waste gas and waste liquid treatment and heat recovery device Download PDFInfo
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- CN209978057U CN209978057U CN201920388730.1U CN201920388730U CN209978057U CN 209978057 U CN209978057 U CN 209978057U CN 201920388730 U CN201920388730 U CN 201920388730U CN 209978057 U CN209978057 U CN 209978057U
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Abstract
The utility model relates to a waste gas, waste liquid treatment and heat reclamation device, including combustion chamber, turbulent flow chamber, steady flow chamber and the heat recovery room that communicates in proper order, the combustion chamber be a cavity, two high temperature nozzle and a combustion head have on the cavity, turbulent flow chamber be a cylinder passageway, the cross-sectional area of passageway all is less than the cross-sectional area of combustion chamber and steady flow chamber for form the venturi effect, steady flow chamber be a cavity, the heat recovery room shell and tube formula heat transfer structure has, including heat transfer tubulation and heat transfer casing, water inlet and steam outlet have on the heat transfer casing, combustion chamber and steady flow chamber pass through turbulent flow chamber intercommunication, steady flow chamber and heat transfer tubulation one side intercommunication. The utility model has large treatment capacity, can treat waste gas and waste liquid simultaneously, and effectively recover the generated heat energy; the occupied area is small, the investment is low, and the method is suitable for treating waste gas and waste liquid of medium and small enterprises; the equipment is easy to process, simple in structure and convenient to use, and has important significance for improving the environmental control capability.
Description
Technical Field
The utility model belongs to the technical field of waste gas, waste liquid treatment and heat recovery and specifically relates to a waste gas, waste liquid treatment and heat recovery device.
Background
A large amount of combustible gas and organic waste liquid are easily generated in the industries of chemical industry, medicine, mechanical spraying, printing and the like, and the waste gas and the waste liquid are respectively treated in the industry. The large and medium-sized enterprises can separately treat the wastes according to the properties of the wastes due to the scale effect and the capital advantage. However, for small and micro enterprises, a professional waste treatment mechanism is often required for treatment due to the small generation amount of waste gas and waste liquid; however, due to the fact that management of many small and micro enterprises is not standard and the capital is short, the environmental pollution is seriously damaged by adopting methods such as steal and emission.
The thermal incineration of waste gas and waste liquid is a common treatment mode, the incineration can decompose the waste gas and waste liquid into inorganic substances, and a large amount of heat energy existing in the burnt flue gas can be recycled.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a can fully burn to waste gas waste liquid to waste gas, waste liquid treatment and heat reclamation device of waste gas waste liquid heat energy can effectively be utilized.
In order to achieve the purpose, the device for treating the waste gas and the waste liquid and recovering the heat comprises a combustion chamber, a turbulent flow chamber, a steady flow chamber and a heat recovery chamber which are sequentially communicated, wherein,
the combustion chamber is a cavity, two high-temperature spray heads and a combustion head are arranged on the cavity,
the turbulent chamber is a cylindrical channel, the cross-sectional area of the channel is smaller than that of the combustion chamber and the steady flow chamber to form a Venturi effect,
the flow stabilizing chamber is a cavity body,
the heat recovery chamber is provided with a shell-and-tube heat exchange structure and comprises heat exchange tubes and a heat exchange shell, the heat exchange shell is provided with a water inlet and a steam outlet,
the combustion chamber is communicated with the flow stabilizing chamber through the turbulent chamber, and the flow stabilizing chamber is communicated with one side of the heat exchange tubes.
The utility model has large treatment capacity, can treat waste gas and waste liquid simultaneously, and effectively recover the generated heat energy; the occupied area is small, the investment is low, and the method is suitable for treating waste gas and waste liquid of medium and small enterprises; the equipment is easy to process, simple in structure and convenient to use, and has important significance for improving the environmental control capability.
Drawings
Fig. 1 is a schematic top view of an exhaust gas/waste liquid treatment and heat recovery apparatus.
Fig. 2 is a schematic view of one side of the heat recovery chamber.
FIG. 3 is a schematic diagram of an internal structure of the waste gas and liquid treatment and heat recovery apparatus.
FIG. 4 is a schematic view of the structure of the waste gas and liquid treatment and heat recovery apparatus.
In the figure: 1. the device comprises a combustion chamber, 2 a turbulence chamber, 3 a steady flow chamber, 4 a heat recovery chamber, 5 a combustion head, 6 a high-temperature spray head, 7 a deionized water inlet, 8 a steam outlet, 9 a flue gas outlet and 10 a heat exchange tube nest.
Detailed Description
The present invention is further described below with reference to the following drawings, which are only for illustration and are not intended to limit the scope of the present invention.
The structure of the waste gas and liquid treatment and heat recovery device of the embodiment is shown in fig. 4, and comprises a combustion chamber, a turbulent flow chamber, a steady flow chamber and a heat recovery chamber which are sequentially communicated, and the internal structure of the device is shown in fig. 3, wherein
The combustion chamber is a cavity, two high-temperature nozzles and a combustion head are arranged on the cavity, waste gas and waste liquid can be conveyed to the high-temperature nozzles through an external pipeline to be sprayed into the combustion chamber, natural gas is conveyed to the combustion head through the external pipeline to be sprayed into the combustion chamber, the natural gas and the waste liquid are combusted together in the combustion chamber, the temperature of the combustion chamber is controlled to operate between 700 ℃ and 1200 ℃ according to the properties of different waste gas and waste liquid, and the temperature of the combustion chamber can be adjusted according to the flow of the natural gas.
The turbulent chamber is a cylindrical channel, two ends of the turbulent chamber are respectively communicated with the combustion chamber and the flow stabilizing chamber, the cross section area of the channel is smaller than that of the combustion chamber and the flow stabilizing chamber, so that a Venturi effect is formed, waste gas and waste liquid are initially combusted in the combustion chamber to be changed into a gas mixture with complex components, and the gas mixture is uniformly mixed under the turbulence action of the turbulent chamber and then enters the flow stabilizing chamber.
The steady flow chamber is a cavity, and the steady flow chamber mainly has the effect of ensuring that the high-temperature flue gas can have sufficient residence time so as to ensure the sufficiency of combustion.
The heat recovery chamber is provided with a shell-and-tube heat exchange structure and comprises a heat exchange tube array and a heat exchange shell, the heat exchange shell is provided with a water inlet and a steam outlet, and the flow stabilizing chamber is communicated with one side of the heat exchange tube array of the shell-and-tube heat exchange structure. The heat recovery chamber is similar to a waste heat boiler structure, and high-temperature flue gas passes through the deionized water of heat exchange shell and tube heating shell side to produce the required steam of production line, for the security of maintaining the heat recovery chamber, need increase safety measure according to the industrial furnace standard. Deionized water in the heat recovery chamber is added through the water inlet and is discharged through the steam outlet.
The equipment is mainly characterized by small occupied area and low investment, and waste gas and waste liquid can be treated in a set of device, so that the characteristics of low investment and high equipment treatment capacity of medium and small companies are solved; the turbulent chamber of the equipment adopts a Venturi structure, so that the waste gas after combustion is burnt without bias flow and dead angles, and the destruction removal rate of organic matters reaches more than 99.99 percent; the waste liquid and waste gas with small discharge capacity are treated in one device, so that the utilization efficiency of the furnace body is greatly improved, and the energy-saving effect of the equipment is obviously improved; the reasonable waste heat utilization system reduces the comprehensive cost of waste gas combustion treatment to the minimum, occupies small area and can be arranged in a container to be conveniently moved.
Claims (1)
1. A waste gas and waste liquid treatment and heat recovery device is characterized by comprising a combustion chamber, a turbulent flow chamber, a steady flow chamber and a heat recovery chamber which are sequentially communicated, wherein,
the combustion chamber is a cavity, two high-temperature spray heads and a combustion head are arranged on the cavity,
the turbulent chamber is a cylindrical channel, the cross-sectional area of the channel is smaller than that of the combustion chamber and the steady flow chamber to form a Venturi effect,
the flow stabilizing chamber is a cavity body,
the heat recovery chamber is provided with a shell-and-tube heat exchange structure and comprises heat exchange tubes and a heat exchange shell, the heat exchange shell is provided with a water inlet and a steam outlet,
the combustion chamber is communicated with the flow stabilizing chamber through the turbulent chamber, and the flow stabilizing chamber is communicated with one side of the heat exchange tubes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201920388730.1U CN209978057U (en) | 2019-03-26 | 2019-03-26 | Waste gas and waste liquid treatment and heat recovery device |
Applications Claiming Priority (1)
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CN201920388730.1U CN209978057U (en) | 2019-03-26 | 2019-03-26 | Waste gas and waste liquid treatment and heat recovery device |
Publications (1)
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CN209978057U true CN209978057U (en) | 2020-01-21 |
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CN201920388730.1U Active CN209978057U (en) | 2019-03-26 | 2019-03-26 | Waste gas and waste liquid treatment and heat recovery device |
Country Status (1)
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CN (1) | CN209978057U (en) |
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2019
- 2019-03-26 CN CN201920388730.1U patent/CN209978057U/en active Active
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