High-efficiency recovery equipment for tail gas of white spirit brewing steaming beam wine steamer
By integrating a steam compressor TGR forced direct heat exchange circulation device and a pressurized isolation purifier, the energy waste and environmental pollution problems in the treatment of the tail gas of the distillation chamber in baijiu brewing are solved, heat recovery and pollutant purification are achieved, adapting to the needs of different brewing processes and simplifying the treatment process.
Patent Information
- Application Number
- CN202511569654.0
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2025-10-30
- Publication Date
- 2026-01-09
AI Technical Summary
In the existing technology, the tail gas treatment method of the distillation process in the liquor brewing industry has problems such as energy waste, environmental pollution and high equipment complexity, and poor adaptability to different brewing processes and raw material ratios.
It adopts an integrated equipment including a steam compressor TGR forced direct heat exchange circulation device, a pressure boosting and isolation purifier and a circulating water supply system. Through forced compression, heat exchange, condensation and multi-layer filtration, it realizes heat recovery, water vapor removal and pollutant purification in the exhaust gas, and adapts to the needs of different brewing processes and raw material ratios.
It achieves efficient recovery and reuse of heat in exhaust gas, reduces environmental pollution, simplifies the treatment process, reduces environmental pressure, and improves the adaptability and processing efficiency of the equipment.
Smart Images
Figure CN121297564A_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The present application belongs to the field of tail gas recovery, and particularly relates to a high-efficiency tail gas recovery equipment for distilling wine. BACKGROUND
[0002] At present, the treatment method for tail gas of distilling wine in the wine brewing industry is relatively simple and extensive. Most enterprises only directly discharge the tail gas into the atmosphere, and this treatment method has many problems. On the one hand, a large amount of water vapor in the tail gas carries a large amount of heat, and direct discharge will cause serious waste of energy, which does not meet the current development requirements of energy saving and emission reduction. On the other hand, the volatile organic compounds and dust contained in the tail gas will cause serious pollution to the surrounding environment, affect the air quality, and harm human health.
[0003] Some enterprises try to simply treat the tail gas of distilling wine, for example, using an ordinary spray tower for cooling treatment. The low spray tower directly contacts the cooling water with the waste gas for heat exchange to achieve the purpose of cooling, but the effect of recycling the heat in the tail gas is very poor, and most of the heat is lost with the discharge of the cooling water. At the same time, the ordinary spray tower has limited effect on the removal of pollutants in the tail gas, and it is difficult to effectively remove volatile organic compounds and fine dust in the tail gas, so the discharged tail gas after treatment may still be over standard.
[0004] In addition, for the treatment of water vapor in the tail gas, although the existing technology uses condensation, adsorption and other methods to remove water in the waste gas, for example, using a condensing device to reduce the temperature of the waste gas below the dew point to condense water vapor into water and discharge, thereby reducing the humidity of the waste gas, but these water removal methods are usually independently set, and are disconnected with the heat recovery, pollutant removal and other process links of the tail gas, resulting in high equipment complexity, complicated treatment process and high operation cost of the whole tail gas treatment system. Moreover, most of the existing treatment equipment can only treat a specific type of tail gas, and has poor adaptability to tail gas generated by different brewing processes and different raw material ratios, and the application range is limited. SUMMARY
[0005] The present application mainly solves the above technical problems.
[0006] To solve the above problems, the technical scheme adopted by the present application is as follows: the high-efficiency tail gas recovery equipment for distilling wine proposed by the present application comprises, in sequence, a sorghum steaming pot, a sorghum retort, a steam compressor TGR forced direct heat exchange circulating device, and a pressurized isolation purifier, and further comprises a circulating water supply system connected with the steam compressor TGR forced direct heat exchange circulating device, and the pressurized isolation purifier is provided with a non-condensed steam discharge port and a discharge port.
[0007] Further, the steam compressor TGR forced direct heat exchange circulation device comprises a compressor body and a heat exchange chamber, the gas inlet end of the compressor body is connected with the tail gas outlet of the sorghum wine retort, the gas outlet end of the compressor body is connected with the inlet of the heat exchange chamber, the circulating water inlet and the circulating water outlet of the heat exchange chamber are connected with the circulating water supply system respectively, and the outlet of the heat exchange chamber is connected with the inlet of the pressurized isolation purifier.
[0008] Further, a plurality of heat exchange pipes are arranged in the heat exchange chamber, the two ends of the heat exchange pipes are communicated with the circulating water inlet and the circulating water outlet respectively, and the heat exchange pipes are distributed in a spiral shape in the heat exchange chamber.
[0009] Further, the pressurized isolation purifier is provided with a filter layer and a pressurizing mechanism, the filter layer is arranged at the inlet end of the pressurized isolation purifier, the pressurizing mechanism is arranged between the filter layer and the non-condensable gas discharge port, and the discharge port is arranged at the bottom of the pressurized isolation purifier.
[0010] Further, the filter layer comprises an initial filter layer, a medium filter layer and a high-efficiency filter layer arranged in sequence, the initial filter layer adopts a metal filter screen, the medium filter layer adopts an activated carbon filter screen, and the high-efficiency filter layer adopts a HEPA filter screen.
[0011] Further, a temperature detection device and a control device are further arranged, the temperature detection device is arranged at the tail gas outlet of the sorghum wine retort and the outlet of the steam compressor TGR forced direct heat exchange circulation device, the temperature detection device is electrically connected with the control device, and the control device is electrically connected with the steam compressor TGR forced direct heat exchange circulation device and the circulating water supply system.
[0012] Further, a tail gas temperature threshold range is preset in the control device, when the temperature detection device detects that the temperature at the tail gas outlet of the sorghum wine retort is higher than the preset upper limit value or the temperature at the outlet of the steam compressor TGR forced direct heat exchange circulation device is higher than the preset upper limit value, the control device controls the steam compressor TGR forced direct heat exchange circulation device to increase the compression power or controls the circulating water supply system to increase the circulating water supply amount.
[0013] Further, the circulating water supply system comprises a circulating water tank, a circulating water pump and a cooling tower, the outlet of the circulating water tank is connected with the circulating water inlet of the steam compressor TGR forced direct heat exchange circulation device through the circulating water pump, the circulating water outlet of the steam compressor TGR forced direct heat exchange circulation device is connected with the inlet of the cooling tower, and the outlet of the cooling tower is connected with the inlet of the circulating water tank.
[0014] Further, the corn steamer is connected with the corn wine retort through a pipeline, and a valve is arranged on the pipeline to control the speed of corn entering the corn wine retort from the corn steamer.
[0015] Further, a condensation and water removal device is further included, which is arranged between the steam compressor TGR forced direct heat exchange circulation device and the pressurized isolation purifier, and includes a condensation cavity and a water outlet, wherein the inlet of the condensation cavity is connected with the outlet of the steam compressor TGR forced direct heat exchange circulation device, the outlet of the condensation cavity is connected with the inlet of the pressurized isolation purifier, and the water outlet is arranged at the bottom of the condensation cavity.
[0016] The beneficial effects achieved by the present application with the above structure are as follows:
[0017] 1. The white liquor brewing steam beam wine tail gas efficient recovery equipment provided by the present application can forcibly compress and efficiently heat exchange the steam beam wine tail gas through the steam compressor TGR forced direct heat exchange circulation device, fully recovers the heat carried in the tail gas, and transfers the heat to the circulating water, so that the heated circulating water can be used in other process links of white liquor brewing, thereby realizing the recycling of energy. Meanwhile, the condensation and water removal device can recover the water vapor in the tail gas, and the generated condensed water can be used for production again, thereby improving the utilization rate of water resources.
[0018] 2. The white liquor brewing steam beam wine tail gas efficient recovery equipment provided by the present application is provided with a multi-layer filtering structure in the pressurized isolation purifier, and the primary efficiency filtering layer, the medium efficiency filtering layer and the high efficiency filtering layer can remove dust, volatile organic compounds and other pollutants in the tail gas step by step. Through effective tail gas treatment, the enterprise can reduce the pollution to the surrounding environment, reduce the environmental protection pressure, avoid facing punishment due to environmental protection problems, and ensure the sustainable development of the enterprise.
[0019] 3. The white liquor brewing steam beam wine tail gas efficient recovery equipment provided by the present application integrates the functions of tail gas collection, heat exchange, water removal and purification in one set of equipment, and forms a complete tail gas treatment process, without the need of dispersively arranging each treatment link, thereby simplifying the tail gas treatment process.
[0020] 4. The white liquor brewing steam beam wine tail gas efficient recovery equipment provided by the present application is provided with an adjustable steam compressor TGR forced direct heat exchange circulation device and a pressurized isolation purifier with a multi-layer filtering structure, which can adjust the compression power of the steam compressor, the supply amount of circulating water and the use state of the filtering layer through the control device according to the temperature, composition, humidity and other characteristics of the tail gas generated by different brewing processes and different raw material ratios, so as to adapt to the treatment requirements of different types of tail gas. BRIEF DESCRIPTION OF DRAWINGS
[0021] Figure 1 A simplified schematic diagram of the overall device of the present application.
[0022] The accompanying drawings are used to provide a further understanding of the present application, and constitute a part of the specification, which together with the embodiments of the present application, are used to explain the present application, and do not constitute a limitation of the present application. DETAILED DESCRIPTION
[0023] The technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the accompanying drawings of the embodiments of the present application. Obviously, the described embodiments are only a part of the embodiments of the present application, rather than all the embodiments of the present application. Based on the embodiments in the present application, all other embodiments obtained by those of ordinary skill in the art without creative work fall within the scope of the present application.
[0024] As Figure 1 shown, the present application proposes a high-efficiency tail gas recycling device for liquor brewing, which comprises, in sequence, a sorghum steaming pot, a sorghum wine retort, a steam compressor TGR forced direct heat exchange circulating device, a condensation water removal device, and a pressurized isolation purifier, and further comprises a circulating water supply system, a temperature detection device, and a control device.
[0025] The sorghum steaming pot and the sorghum wine retort are connected by a pipeline, and a valve is arranged on the pipeline. The valve is used to control the speed of sorghum entering the sorghum wine retort from the sorghum steaming pot. The opening degree of the valve can be adjusted according to the processing progress of the sorghum wine retort, so as to ensure that the cooking and processing of sorghum in the sorghum wine retort are stably carried out.
[0026] The steam compressor TGR forced direct heat exchange circulating device comprises a compressor body and a heat exchange chamber. The gas inlet end of the compressor body is connected with the tail gas outlet of the sorghum wine retort by a pipeline, and is used to receive the tail gas generated by the sorghum wine retort. The gas outlet end of the compressor body is connected with the inlet of the heat exchange chamber. The compressor body can compress the tail gas, so as to increase the pressure and temperature of the tail gas, and facilitate the subsequent heat exchange process. A plurality of heat exchange pipes are arranged in the heat exchange chamber in a spiral manner. The two ends of the heat exchange pipes are respectively connected with the circulating water inlet and the circulating water outlet of the heat exchange chamber. The spiral arrangement of the heat exchange pipes can increase the contact area and contact time of the circulating water and the tail gas, and improve the heat exchange efficiency.
[0027] The circulating water supply system comprises a circulating water tank, a circulating water pump, and a cooling tower. The outlet of the circulating water tank is connected with the circulating water inlet of the heat exchange chamber through the circulating water pump, and the circulating water pump provides power for the flow of the circulating water. The circulating water outlet of the heat exchange chamber is connected with the inlet of the cooling tower. The circulating water that has absorbed heat enters the cooling tower for cooling treatment. The outlet of the cooling tower is connected with the inlet of the circulating water tank. The cooled circulating water reenters the circulating water tank, so as to realize the recycling of the circulating water.
[0028] The condensing and water removing device is arranged between the steam compressor TGR forced direct heat exchange circulation device and the booster isolation purifier, and comprises a condensing cavity and a water outlet. The inlet of the condensing cavity is connected with the outlet of the heat exchange chamber through a pipeline, and the outlet of the condensing cavity is connected with the inlet of the booster isolation purifier through a pipeline. A condensing pipe (not shown in the figure) is arranged in the condensing cavity, cooling liquid is introduced into the condensing pipe, the temperature of the tail gas entering the condensing cavity can be reduced below the dew point, the water vapor in the tail gas is condensed into liquid water, and the condensed water is discharged from the water outlet arranged at the bottom of the condensing cavity and can be collected for use in the cleaning process of sorghum and the like.
[0029] The booster isolation purifier is provided with a filter layer and a booster mechanism. The filter layer is arranged at the inlet end of the booster isolation purifier and comprises an initial filter layer, a medium filter layer and a high-efficiency filter layer arranged in sequence. The initial filter layer adopts a metal filter screen for filtering dust with a larger particle size in the tail gas. The medium filter layer adopts an activated carbon filter screen for adsorbing volatile organic compounds in the tail gas and removing odors. The high-efficiency filter layer adopts a HEPA filter screen for filtering fine dust and microorganisms in the tail gas. The booster mechanism is arranged between the filter layer and the non-condensable steam discharge port and adopts a booster fan to increase the pressure of the tail gas and facilitate the smooth discharge of the purified non-condensable steam from the non-condensable steam discharge port arranged at the top of the booster isolation purifier. The bottom of the booster isolation purifier is provided with a discharge port for discharging impurities filtered by the filter layer and condensed water.
[0030] The temperature detection device comprises a first temperature sensor and a second temperature sensor. The first temperature sensor is arranged at the tail gas outlet of the sorghum wine retort for detecting the temperature of the tail gas discharged by the sorghum wine retort. The second temperature sensor is arranged at the outlet of the heat exchange chamber of the steam compressor TGR forced direct heat exchange circulation device for detecting the temperature of the tail gas after heat exchange. The temperature detection device is electrically connected with the control device to transmit the detected temperature signal to the control device.
[0031] The control device adopts a PLC controller and is electrically connected with the compressor body of the steam compressor TGR forced direct heat exchange circulation device, the circulating water pump of the circulating water supply system and the booster mechanism of the booster isolation purifier. The control device is pre-set with a tail gas temperature threshold range, for example, the upper limit of the temperature at the tail gas outlet of the sorghum wine retort is ℃, and the upper limit of the temperature at the outlet of the heat exchange chamber is ℃. When the first temperature sensor detects that the temperature at the tail gas outlet of the sorghum wine retort is higher than ℃ or the second temperature sensor detects that the temperature at the outlet of the heat exchange chamber is higher than ℃, the control device controls the compressor body to increase the compression power to improve the compression effect of the tail gas or controls the circulating water pump to increase the circulating water supply to improve the heat exchange efficiency, so that the temperature of the tail gas is reduced to the pre-set threshold range.
[0032] The working process of the device for efficiently recycling tail gas of a liquor brewing retort is as follows:
[0033] S1: After the sorghum is cooked in the sorghum steamer, the valve is opened, the sorghum is transported to the sorghum still through the pipeline for subsequent processing, and the sorghum still generates tail gas during the processing.
[0034] S2: The tail gas generated by the sorghum still enters the compressor body of the steam compressor TGR forced direct heat exchange circulating device through the pipeline, the compressor body compresses the tail gas to increase the pressure and temperature of the tail gas.
[0035] S3: The compressed tail gas enters the heat exchange chamber, and at the same time, the circulating water pump of the circulating water supply system transports the circulating water in the circulating water tank to the heat exchange pipe in the heat exchange chamber, the tail gas exchanges heat with the circulating water in the heat exchange pipe in the heat exchange chamber, the heat in the tail gas is transferred to the circulating water, the circulating water absorbs heat and the temperature rises, and the cooled circulating water returns to the circulating water tank for repeated use.
[0036] S4: The tail gas after heat exchange is discharged from the outlet of the heat exchange chamber and enters the condensing cavity of the condensing and dehydrating device, the condensing pipe in the condensing cavity cools the tail gas, and the water vapor in the tail gas is condensed into liquid water, and the condensed water is discharged from the drain and collected for recycling.
[0037] S5: The dehydrated tail gas is discharged from the outlet of the condensing cavity and enters the booster isolation purifier, and is filtered by the primary filter layer, the medium filter layer and the high-efficiency filter layer in the filter layer in sequence to remove dust, volatile organic compounds and other pollutants in the tail gas.
[0038] S6: The filtered tail gas is pressurized by the booster mechanism and then discharged from the non-condensable gas discharge port to meet the emission standard, and the impurities and condensed water generated during the filtration process are discharged from the discharge port.
[0039] S7: During the entire working process, the temperature detection device detects the tail gas temperature in real time and transmits the temperature signal to the control device, the control device automatically adjusts the compression power of the compressor body and the circulating water supply amount of the circulating water pump according to the temperature signal, and ensures stable and efficient operation of the equipment.
[0040] The above describes the present application and its embodiments, which are not restrictive, and the drawings shown are only one of the embodiments of the present application, and the actual structure is not limited thereto. In general, if a person skilled in the art is inspired thereby, without departing from the purpose of the present application, without creative design, similar structure and embodiments of the technical solution can be designed, which shall belong to the protection scope of the present application.
Claims
1. A high-efficiency recovery device for tail gas from the distillation chamber in Baijiu brewing, characterized in that: The device includes a sorghum steamer, a sorghum distillation still, a TGR forced direct heat exchange circulation device, and a pressurization isolation purifier connected in sequence. It also includes a circulating water supply system connected to the TGR forced direct heat exchange circulation device. The pressurization isolation purifier is equipped with a non-condensable steam discharge port and a clean discharge port.
2. The high-efficiency recovery equipment for tail gas from the distillation process of Baijiu brewing as described in claim 1, characterized in that: The steam compressor TGR forced direct heat exchange circulation device includes a compressor body and a heat exchange chamber. The air inlet of the compressor body is connected to the exhaust outlet of the sorghum distillation still, the air outlet of the compressor body is connected to the inlet of the heat exchange chamber, the circulating water inlet and circulating water outlet of the heat exchange chamber are respectively connected to the circulating water supply system, and the outlet of the heat exchange chamber is connected to the inlet of the pressurized isolation purifier.
3. The high-efficiency recovery equipment for tail gas from the distillation process of Baijiu brewing, as described in claim 2, is characterized in that: The heat exchange chamber is provided with a number of heat exchange tubes, the two ends of which are connected to the circulating water inlet and the circulating water outlet, respectively, and the heat exchange tubes are distributed in a spiral shape in the heat exchange chamber.
4. The high-efficiency recovery equipment for tail gas from the distillation chamber of baijiu brewing as described in claim 1, characterized in that: The pressurized isolation purifier is equipped with a filter layer and a pressurization mechanism. The filter layer is located at the inlet end of the pressurized isolation purifier, the pressurization mechanism is located between the filter layer and the non-condensable steam discharge port, and the exhaust port is located at the bottom of the pressurized isolation purifier.
5. The high-efficiency recovery equipment for tail gas from the distillation process of Baijiu brewing as described in claim 4, characterized in that: The filter layer includes a pre-filter layer, a medium-efficiency filter layer and a high-efficiency filter layer arranged in sequence. The pre-filter layer uses a metal filter screen, the medium-efficiency filter layer uses an activated carbon filter screen, and the high-efficiency filter layer uses a HEPA filter screen.
6. The high-efficiency recovery equipment for tail gas from the distillation process of Baijiu brewing as described in claim 1, characterized in that: It also includes a temperature detection device and a control device. The temperature detection device is located at the tail gas outlet of the sorghum still and at the outlet of the steam compressor TGR forced direct heat exchange circulation device. The temperature detection device is electrically connected to the control device, and the control device is electrically connected to the steam compressor TGR forced direct heat exchange circulation device and the circulating water supply system.
7. The high-efficiency recovery equipment for tail gas from the distillation chamber of baijiu brewing as described in claim 6, characterized in that: The control device has a preset exhaust gas temperature threshold range. When the temperature detection device detects that the temperature at the exhaust gas outlet of the sorghum still is higher than the preset upper limit or the temperature at the outlet of the steam compressor TGR forced direct heat exchange circulation device is higher than the preset upper limit, the control device controls the steam compressor TGR forced direct heat exchange circulation device to increase the compression power or controls the circulating water supply system to increase the circulating water supply.
8. The high-efficiency recovery equipment for tail gas from the distillation process of Baijiu brewing as described in claim 1, characterized in that: The circulating water supply system includes a circulating water tank, a circulating water pump, and a cooling tower. The outlet of the circulating water tank is connected to the circulating water inlet of the steam compressor TGR forced direct heat exchange circulation device through the circulating water pump. The circulating water outlet of the steam compressor TGR forced direct heat exchange circulation device is connected to the inlet of the cooling tower, and the outlet of the cooling tower is connected to the inlet of the circulating water tank.
9. The high-efficiency recovery equipment for tail gas from the distillation process of Baijiu brewing as described in claim 1, characterized in that: The sorghum steamer and the sorghum still are connected by a pipe, and the pipe is equipped with a valve to control the speed at which sorghum enters the sorghum still from the sorghum steamer.
10. The high-efficiency recovery equipment for tail gas from the distillation process of Baijiu brewing according to any one of claims 1-9, characterized in that: It also includes a condensate removal device, which is located between the steam compressor TGR forced direct heat exchange cycle device and the pressurized isolation purifier. The condensate removal device includes a condensation chamber and a drain outlet. The inlet of the condensation chamber is connected to the outlet of the steam compressor TGR forced direct heat exchange cycle device, and the outlet of the condensation chamber is connected to the inlet of the pressurized isolation purifier. The drain outlet is located at the bottom of the condensation chamber.