WO2019157784A1

WO2019157784A1 - Automated production line whole-process monitoring method for herb fiber biological refining

Info

Publication number: WO2019157784A1
Application number: PCT/CN2018/086427
Authority: WO
Inventors: 刘正初; 苏维利; 李云峰
Original assignee: 大庆天之草生物新材料科技有限公司
Priority date: 2018-02-13
Filing date: 2018-05-11
Publication date: 2019-08-22
Also published as: CN108387267B; CN108387267A

Abstract

The present invention provides an automated production line whole-process monitoring method for herb fiber biological refining, comprising the following solution: by means of a control center, controlling, on the basis of a line speed configured by the control center, the operation of a material transportation mechanism of a preprocessing device, a material transportation mechanism of a seeding device, a material transportation mechanism of a fermentation device, a material transportation mechanism of a sterilization device, a material transportation mechanism of a water treatment device, a material transportation mechanism of an oil dipping device, a material transportation mechanism of a drying device, a material transportation mechanism of an opening and loosening device, a material transportation mechanism of a packing device, and a material transportation mechanism between the above adjacent devices, such that the speeds of preprocessing, seeding, fermentation, sterilization, water treatment, oil dipping, drying, opening and loosening and packing are coordinated and consistent, realizing seamless connection between adjacent processes. The present invention resolves the technical issues in the prior art for a herb fiber biological refining process in which devices operate in different speeds and the supply of required materials is not coordinated.

Description

Full-process monitoring method for automatic production line of herbal fiber biorefinery

Technical field

The invention relates to the field of hemp fiber production. Specifically, it is a whole process monitoring method for an automated production line of herbal fiber biorefinery.

Background technique

Herb fiber is derived from ramie, kenaf, jute, hemp, flax, sisal, abaca, pineapple, apocynum, reed, awning, and asparagus. Ramat, kenaf, jute, hemp bast, initially processed flax stems, reed stems, and crop straw (such as straw) or similar waste (such as bagasse) with a cellulose content of more than 25% ). Herb fiber is associated with more than 25% of non-cellulose, which must be stripped by appropriate methods, so that natural cellulose fibers can be widely used as the basic materials for textile, paper, biomass materials, biomass energy and other manufacturing industries. Among them, some tissue-type non-cellulose (such as ramie, kenaf, jute, hemp bone, sisal mesophyll) can be stripped by primary processing of agricultural machinery; water-soluble non-cellulose (protein, various monosaccharides and starch) Polysaccharides can be removed by water swelling; bonded non-cellulosics (including pectin, hemicellulose, lignin, etc.) that are directly or indirectly linked to cellulose by chemical bonds must pass very complex chemical or biochemical reactions. The process can be stripped.

The Institute of Materia Medica of the Chinese Academy of Agricultural Sciences has developed a patent for the problem of serious environmental pollution caused by the "ramie" and "chemical degumming/pulping" methods. A functional strain is used for industrial fermentation to rapidly extract herbal fiber. Method (Patent No.: ZL201110410078.7). The technical scheme of the invention patent is at the international leading level in the similar research in the aspects of high-efficiency strain breeding and complex enzyme catalytic mechanism. Despite this, the invention still has many drawbacks such as mismatch of process equipment, excessive manual operation, and inadequate technical measures or unstable product quality.

Heilongjiang Tianzhicao Hema New Material Technology Co., Ltd. A system and method for automatically operating bio-refined herbal fiber (patent application number: 201710398620.9) and a method and equipment for recycling and utilizing waste liquid of herbal fiber bio-refining process (patent application) No.: 201710840524.5) and a series of techniques, overcoming the shortcomings of the method of rapid extraction of herbal fiber by factory fermentation, "there are too many manual operations, resulting in inadequate technical measures or unstable product quality". However, due to the lack of perfect control equipment, the operation of each equipment is not synchronized and the required supply of materials is not coordinated.

Summary of the invention

The technical problem solved by the invention is to overcome the shortcomings of the unsynchronized operation of various equipments in the prior art herbal fiber bioremediation process and the uncoordinated supply of materials, and to provide a whole process monitoring method for the automatic production line of herbal fiber biorefinery.

The whole process monitoring method for the automatic production line of herbal fiber biorefining of the invention, the material conveying mechanism of the pretreatment equipment, the material conveying mechanism of the inoculating equipment, the material conveying mechanism of the fermentation equipment, the material conveying mechanism of the inactivation equipment, and the water treatment equipment are controlled by the control center The material transfer mechanism, the material transport mechanism of the oil-sucking equipment, the material transport mechanism of the drying equipment, the material transport mechanism of the opening equipment, the material transport mechanism of the packaging equipment, and the material transfer mechanism between the adjacent equipments according to the control center The set line speed operation aligns the speeds of pretreatment, inoculation, fermentation, inactivation, water, oil, drying, opening and packaging and achieves a seamless connection between adjacent processes.

Preferably, the pretreatment device and/or the inoculation device and/or the fermentation device and/or the inactivation device and/or the water treatment device and/or the oil extraction device and/or the drying device and/or the opening device are monitored by a camera. The material transfer status of the device, when the control center receives the fault signal sent by the camera, issues a forced brake command to control each device to automatically stop running.

Preferably, the camera disposed at the beginning of the material transport mechanism of the fermentation device and the middle and rear segments thereof can also be used to monitor the process mature mark of the fermentation product. When the process mature mark appears earlier than the set time, the control center controls the material transfer mechanism of the fermentation device. The material transfer mechanism of the inactivation equipment, the material transport mechanism of the water treatment equipment, the material transport mechanism of the oil staining equipment, the material transport mechanism of the drying equipment, and the material transport mechanism of the opening equipment increase the plastic transmission speed; Appearing at the set time, the control center controls the material transport mechanism of the fermentation equipment, the material transport mechanism of the inactivation equipment, the material transport mechanism of the water treatment equipment, the material transport mechanism of the oil staining equipment, the material transport mechanism of the drying equipment, and the opening of the material. The material transfer mechanism of the equipment reduces the material transfer speed; when the process mature mark returns to the set time, the control center controls the material transfer mechanism of the fermentation equipment, the material transfer mechanism of the inactivation equipment, the material transfer mechanism of the water treatment equipment, and the oil stain Material transfer mechanism of equipment, material transfer of drying equipment Material handling equipment agency bodies and opening speed of recovery of the original set.

Preferably, the control unit controls the bacterial liquid sprinkling device of the inoculation device, the steam supply device of the fermentation device, the hot water supply device of the inactivation device, the cold water supply device of the water treatment device, and the fuel injection device of the oil splashing device according to the control center. The set amount is supplied with bacterial liquid, steam, hot water, cold water and emulsified oil.

Preferably, the fermentation device and/or the inactivation device and/or the oiling device and/or the drying device and/or the opening device and/or the emulsified oil mixing tank and/or the hot water recovery tank are monitored by an electronically controlled thermometer. And/or warming the temperature of the tank, the electronically controlled thermometer is in communication with the control center, and when the control center receives the temperature sent by the electronic control thermometer below a set temperature, the open steam flow control is issued. The valve injects steam into the fermentation equipment and/or the inactivation equipment and/or the oiling equipment and/or drying equipment and/or the opening equipment and/or the emulsified oil mixing tank and/or the hot water recovery tank and/or the warm water mixing tank Instructions.

Preferably, the humidity in the fermentation device and/or the drying device and/or the opening device is monitored by an electronically controlled hygrometer, the electronically controlled hygrometer being communicatively coupled to the control center, when the control center receives The dehumidification device of the fermentation device and/or the dehumidification device of the drying device and/or the dehumidification device of the opening device are accelerated to dehumidify or decelerate when the humidity sent by the electronically controlled hygrometer exceeds the set humidity range. Alternatively, the moisture is stopped to maintain the humidity in the fermentation equipment and/or the drying equipment and/or the opening apparatus within a set range.

Preferably, the emulsified oil recovery tank and/or the emulsified oil blending tank and/or the emulsified oil storage tank and/or the tap water storage tank and/or the clean water recovery tank and/or the tap water storage tank and/or the effluent oil storage tank and/or the effluent oil storage tank and/or the water purification tank of the herb fiber biorefining line are electrically controlled. A hot water recovery tank and/or a hot water storage tank and/or a cooling water recovery tank and/or a warm water tank and/or a warm water storage tank monitor the level of the tank liquid, the electronically controlled level gauge communicating with the control center Connecting, when the control center receives the liquid level sent by the electronically controlled liquid level gauge lower than the set liquid level, controlling the inflow valve of each tank and the pump to open the injection liquid to the set liquid level.

Preferably, the water quality of the water treatment wastewater recovery treatment zone of the herbal fiber bioremediation production line and the water quality of the inactivated wastewater recovery treatment zone are monitored in real time by a water quality monitor, and the water quality detector is connected with the control center. The control center issues an alarm message when it receives information that the water quality detector has exceeded the specified water quality.

Preferably, the harmful substance concentration of the integrated exhaust gas discharge port of the herb fiber bio-refining production line is monitored by a harmful gas monitor, and the harmful gas monitor is communicably connected with the control center, and when the control center receives the harmful gas monitoring An alarm message is issued when the concentration of harmful substances from the instrument exceeds the information of the set indicator.

Preferably, the exhaust gas discharged from the integrated exhaust gas exhaust port comprises a hot gas and/or a fermentation device and/or an emulsified oil liquid blending tank and/or an emulsified oil liquid recovery tank formed by the opening device discharging the material through the exhaust fan and cooling the material. / or emulsified oil storage tanks and / or tap water storage tanks and / or clean water recovery tanks and / or hot water recovery tanks and / or hot water storage tanks and / or cooling water recovery tanks and / or warm water tanks and / or warm water The gas discharged from the storage tank and/or the bacterial suspension mixing tank and/or the water treatment waste recovery treatment zone and/or the inactivated waste recovery treatment zone and/or the waste recovery treatment zone and/or the preparation of the strain.

Preferably, the tissue type non-cellulosic material produced by mechanical peeling during the processing of the material by the particle extractor is controlled by the control center.

Preferably, the first flow control valve and the first liquid booster pump for supplying warm water to the inoculating device are controlled by the control center, thereby controlling the ratio of the bacterial liquid to the warm water to sufficiently mix the two to form a bacterial suspension, and controlling The central control second liquid booster pump and the second flow control valve control the bacterial suspension to be input into the inoculating device of the inoculating device according to the set amount, and the bacterial liquid sprinkling device is under the control of the control center The bacterial suspension is sprayed onto the material.

Preferably, the control center controls an air supply flow control valve that supplies steam into the closed casing of the fermentation device, a water supply flow control valve that supplies water to the closed casing, and an atomization device that is connected to the water supply flow control valve, the fermentation The device further includes a thermometer and a hygrometer located in the housing and respectively in communication with the control center, the control center controlling the air supply flow control valve according to the information transmitted by the thermometer, according to the hygrometer The incoming information controls the water supply flow control valve and the atomizing device.

Preferably, a flow control valve, a liquid transfer pump, and a water spray device that supply hot water to the inactivation device are controlled by the control center, and the flow control valve and the liquid transfer pump are quantitatively supplied under the control of the control center. The hot water is sprayed to the material under the control of the control center, and the water quality of the inactivated waste liquid recovery treatment area is detected by a water quality detector, and the water quality detector detects and communicates with the control center. After receiving the information that the water quality of the water quality detector meets the requirements, the control center controls the extraction pump to deliver the treated water to the hot water storage tank.

Preferably, the temperature in the inactivation device of the shutdown production is detected by a thermometer, and the thermometer is communicatively connected to the control center, and the control center controls the spray to the inside of the inactivation device to increase the temperature according to the information transmitted from the thermometer. The device causes the temperature in the inactivation device to reach a set starting temperature.

Preferably, the outflow flow control valve of the tap water storage tank that supplies water to the water treatment device, the liquid booster pump, and the water spray device connected to the outflow flow control valve are controlled by the control center, and the water spray device is in the Spraying water to the material under the control of the control center; the water treatment waste liquid flows to the water treatment waste liquid recovery treatment area for treatment, and the water quality of the water treatment waste liquid recovery treatment area is detected by the water quality detector, when the control center receives When the water quality from the water quality monitor reaches the set requirement information, the inflow flow control valve and the extraction pump of the clean water recovery tank are controlled to deliver the water that meets the set requirements to the clean water recovery tank; when the liquid level in the hot water recovery tank When the liquid level is lower than the control center, the control center controls the inflow flow control valve of the hot water recovery tank to deliver the water that meets the set requirements to the hot water recovery tank.

Preferably, the first flow control valve of the emulsified oil storage tank of the oil slick device, the effluent liquid boosting pump and the fuel injection device connected to the first flow control valve are controlled by a control center, and the fuel injection device is at the control center The emulsified oil is sprayed on the material under the control, and the first extraction pump is controlled by the control center to transport the oil waste liquid to the emulsified oil recovery tank through the one-way control valve, and then the second extraction pump and the second control pump are controlled by the control center. The second flow control valve transports the oil waste liquid in the emulsion recovery tank to the emulsified oil mixing tank, and controls the third air pump and the third flow control valve to control the emulsified oil liquid and the oil waste liquid according to a set ratio. Fully mixed, and the mixed oil is heated to a set temperature by the steam flowing through the steam flow control valve controlled by the control center, and then passed through the fourth extraction pump and the fourth flow controlled by the control center The control valve is delivered to the emulsified oil storage tank for recycling.

Preferably, the temperature in the oil-repellent device for shutdown production is detected by a thermometer, and the thermometer is communicatively connected with the control center, and the control center controls the spray device for spraying the interior of the oil-splatter device to increase the temperature according to the information transmitted by the thermometer. The temperature in the oil slick equipment is brought to the set starting temperature.

Preferably, the flow control valve for supplying steam to the heat exchanger of the drying device and the gas trap, the pump and the one-way control valve for recovering the steam condensed water in the heat exchanger are controlled by the control center, and the steam condensed water passes through The gas trap, the pump and the one-way control valve are recovered to the emulsified oil recovery tank, and the exhaust fan connected to the drying device is controlled by the control center to extract the water vapor formed by the evaporation of the moisture in the material in the drying device. Recover to the hot water recovery tank to the control valve.

Preferably, the softened water extraction pump and the softened water flow control valve for supplying softened water to the emulsified oil blending tank of the opening device are controlled by the control center, and the emulsified oil blending tank also receives the extracting pump flowing through the controlled center. And the emulsified oil stock solution of the flow control valve, the emulsified oil stock solution and the softened water are thoroughly mixed according to the set ratio, and the rated amount of the emulsified oil is controlled by the control center to control the oil flow control valve, the oil liquid booster pump and the fuel injection device. Evenly sprayed onto the material, and the exhaust fan connected to the interior of the opening device is controlled by the control center to discharge the hot air formed by the cooling of the material in the opening device and discharged to the outside of the opening device through the one-way control valve.

Preferably, the first flow control valve is controlled by the control center to cause cooling water from the preparation of the strain and having a certain output pressure to flow into the cooling water recovery tank, and the cooling water is recovered in the tank when the cooling water recovery tank is full. The water is sent to the tap water storage tank, and a one-way control valve is arranged between the cooling water recovery tank and the tap water storage tank to prevent the high water of the tap water storage tank from flowing back to the cooling water recovery tank or returning to the strain that loses the cooling water output pressure. Preparation room

Compared with the prior art, the production process and equipment for continuously supplying the logarithmic growth phase of the present invention have the following beneficial effects:

1. The whole process monitoring method for the automatic production line of herbal fiber bio-refining of the invention, the material transfer mechanism for controlling each device and the material transfer mechanism between adjacent devices are controlled by the control center according to the line speed set by the control center to make pre-treatment and inoculation The speed of fermentation, inactivation, water treatment, oil staining, drying, opening and packaging is consistent and the seamless connection between adjacent processes is achieved. The solution realizes automatic transmission of materials in and between adjacent devices, thereby enabling full automation control of material transmission throughout the production line.

2. Through the linkage of the camera and the control center, an automatic monitoring and coping mechanism for the material delivery failure of the entire production line is established, which greatly saves manpower, and its automatic forced braking can timely prevent the failure of one device from causing damage to other devices.

3. The camera at the beginning of the material transport mechanism and the middle and rear sections of the fermentation equipment can also be used to monitor the process maturity mark of the fermentation product. The linkage between the camera and the control center can adjust the fermentation equipment and the downstream according to the speed of material fermentation. The transfer speed of the material transfer mechanism of each device.

4. The steam, water and oil supply devices of each device are controlled by the control center to supply the liquid, steam, hot water, cold water and emulsified oil according to the amount set by the control center, thereby realizing the fully automated supply of steam and liquid throughout the production line.

5. The temperature of each device is monitored by an electronically controlled thermometer, and when the control center receives the temperature sent by the electronically controlled thermometer below a set temperature, an instruction is issued to open the steam flow control valve to inject steam into the corresponding device. This enables fully automated control of the temperature of the individual equipment throughout the production line.

6. Monitoring the liquid level of each tank liquid by an electronically controlled liquid level meter, and controlling the inflow valve of each tank when the control center receives the liquid level sent by the electronically controlled liquid level gauge below a set liquid level or The pump opens the injected liquid to the set level, enabling fully automated control of the liquid level of all containers throughout the line.

7. Real-time monitoring of the water quality of each area of the herbal fiber biorefinery production line by a water quality monitor. When the water quality meets the set index, the water can be recycled, and when the control center receives the water quality from the water quality detector An alarm message is issued when the information of the set indicator is exceeded.

8. The exhaust gas discharge port of the herb fiber bio-refining production line of the gas monitor is provided with monitoring harmful substances in the exhaust gas, and when the gas meets the set index, it can be discharged to the atmosphere, and when the control center receives the gas monitoring An alarm message is issued when the harmful substance sent by the instrument exceeds the information of the set indicator.

9. In addition, various equipment and areas are monitored through the control center to automatically control the recycling of steam, water and oil within and across the various equipment and areas.

DRAWINGS

1 is a schematic view showing the principle of the whole process monitoring method for the automatic production line of herbal fiber bio-refining according to the first embodiment of the present invention.

Reference numeral

G1 second emulsified oil blending tank, G2 emulsified oil recovery tank, G3 first emulsified oil blending tank, G4 emulsified oil storage tank, G5 tap water storage tank, G6 clean water recovery tank, G7 hot water recovery tank, G8 hot water storage tank, G9 cooling water recovery tank, G10 warm water mixing tank, G11 warm water storage tank, G12 bacteria suspension tank;

Y1 first emulsified oil stock solution, Y2 second emulsified oil stock solution;

J strain preparation room;

K control center;

S1 pretreatment equipment, S2 inoculation equipment, S3 fermentation equipment, S4 inactivation equipment, S5 water treatment equipment, S6 oil storage equipment, S7 drying equipment, S8 opening equipment, S9 packaging equipment;

Q1 inactivated waste liquid recovery and treatment area, Q2 water treatment waste liquid recovery and treatment area, Q3 waste residue recovery and treatment area.

Symbol in the figure

Logistics direction,

Two-way control line,

One-way control valve,

Gas trap,

Flow control valve,

Extraction pump or extractor,

Liquid increases the pump,

Online detector (electrically controlled thermometer, electronically controlled hygrometer or electronically controlled level gauge),

Manual brake button.

Detailed ways

The whole process monitoring method for the automatic production line of herbal fiber bio-refining of the invention has the control principle shown in Fig. 1. The material conveying mechanism of the pretreatment equipment S1, the material conveying mechanism of the inoculating equipment S2, and the material conveying of the fermentation equipment S3 are controlled by the control center K. Mechanism, material conveying mechanism of inactivation equipment S4, material conveying mechanism of water treatment equipment S5, material conveying mechanism of oiling equipment S6, material conveying mechanism of drying equipment S7, material conveying mechanism of opening equipment S8, packaging equipment S9 The material transfer mechanism between the material transfer mechanism and the adjacent equipment is operated according to the line speed set by the control center K to enable pretreatment, inoculation, fermentation, inactivation, water treatment, oil staining, drying, opening and packaging. The speed is coordinated and seamlessly connected between adjacent processes. The solution realizes the automatic transportation of materials in and between adjacent devices, so that the entire production line realizes full automatic control of material transfer.

More specifically, the speed sensor may be disposed in each material conveying mechanism and the material transfer mechanism. When the conveying speed of a material conveying mechanism and the material transferring mechanism exceeds the speed set by the control center K, the control center K adjusts the material conveying mechanism or The drive of the material transfer mechanism, such as the motor, until the data from the speed sensor meets the set range. Alternatively, another solution may be adopted, for example, calculating the running speed of the driving device of each material conveying mechanism and the material transfer mechanism according to the set line speed, such as the rotation speed of the motor, and the control center K controls the motor to control each material according to the calculated speed. The operating speed of the drive mechanism of the transport mechanism and the material transfer mechanism, so that the material transfer mechanism and the material transfer mechanism obtain a coordinated linear velocity.

Monitoring the pretreatment device S1 and/or the inoculation device S2 and/or the fermentation device S3 and/or the inactivation device S4 and/or the water treatment device S5 and/or the oil application device S6 and/or the drying device S7 by means of a camera / or open the material transfer state of the device S8, when the control center K receives the fault signal sent by the camera, a forced brake command is issued to control each device to automatically stop running. Through the linkage of the camera and the control center K, an automatic monitoring and coping mechanism for the material delivery failure of the entire production line is established, which greatly saves manpower, and the automatic forced braking can timely prevent the failure of one device from causing damage to other devices.

The camera at the beginning of the material transport mechanism and the middle and rear segments of the fermentation device S3 can also be used to monitor the process maturity mark of the fermentation product. When the process mature mark appears earlier than the set time, the control center controls the material transfer mechanism of the fermentation device S3, The material conveying mechanism of the inactivation device S4, the material conveying mechanism of the water treatment device S5, the material conveying mechanism of the oiling device S6, the material conveying mechanism of the drying device S7, and the material conveying mechanism of the opening device S8 increase the material conveying speed; The process mature sign appears later than the set time. The control center controls the material transfer mechanism of the fermentation equipment S3, the material transfer mechanism of the inactivation equipment S4, the material transfer mechanism of the water treatment equipment S5, the material transport mechanism of the oil storage equipment S6, and the drying. The material conveying mechanism of the device S7 and the material conveying mechanism of the opening device S8 reduce the material conveying speed; when the process maturity flag is restored to occur at the set time, the control center controls the material conveying mechanism of the fermentation device S3 and the material transmission of the inactivation device S4. Material conveying mechanism of mechanism, water treatment equipment S5, material conveying mechanism of oil staining equipment S6, drying The material conveying mechanism of the device S7 and the material conveying mechanism of the opening device S8 restore the originally set speed. Through the above scheme, the control center can adjust the transmission speed of the material conveying mechanism of the fermentation equipment and the downstream equipment according to the speed of material fermentation.

Controlling the bacterial spray device of the inoculating device S2, the steam supply device of the fermentation device S3, the hot water supply device of the inactivation device S4, the cold water supply device of the water treatment device S5, and the fuel injection device of the oil splashing device S6 by the control center K The bacterial liquid, steam, hot water, cold water and emulsified oil are supplied according to the amount set by the control center K, thereby achieving a fully automated supply of steam and liquid throughout the production line.

Monitoring the fermentation device S3 and/or the inactivation device S4 and/or the oiling device S6 and/or the drying device S7 and/or the opening device S8 and/or the emulsified oil mixing tank and/or hot water by means of an electronically controlled thermometer The temperature of the recovery tank G7 and/or the warm water mixing tank G10, the electronically controlled thermometer is in communication connection with the control center K, when the control center K receives the temperature sent by the electronic control thermometer is lower than the set temperature When the steam flow control valve is opened to the fermentation device S3 and/or the inactivation device S4 and/or the oiling device S6 and/or the drying device S7 and/or the opening device S8 and/or the emulsified oil mixing tank and/or heat The water recovery tank G7 and/or the warm water mixing tank G10 is instructed to inject steam. Monitoring the temperature of each device by an electronically controlled thermometer, and when the control center K receives the temperature sent by the electronically controlled thermometer below a set temperature, issuing an instruction to open the steam flow control valve to inject steam into the corresponding device, thereby Fully automated control of the temperature of the individual equipment throughout the production line.

The humidity in the fermentation device S3 and/or the drying device S7 and/or the opening device S8 is monitored by an electronically controlled hygrometer, the electronically controlled hygrometer being communicatively coupled to the control center K, when the control center K Receiving the dehumidification device of the fermentation device S3 and/or the dehumidification device of the drying device S7 and/or the dehumidification device of the opening device S8 when receiving the humidity sent from the electronically controlled hygrometer exceeds the set humidity range The wet or decelerated moisture is drained or the moisture is stopped to maintain the humidity in the fermentation device S3 and/or the drying device S7 and/or the opening device S8 within a set range. Fully automated control of the humidity of the individual equipment throughout the production line is achieved through the control of the electronically controlled hygrometer and the control center K.

Emulsified oil recovery tank and/or emulsified oil blending tank and/or emulsified oil storage tank and/or tap water storage tank and/or clean water recovery tank and/or hot water recovery of the herbal fiber biorefinery production line by electronically controlled liquid level meter a tank and/or a hot water storage tank and/or a cooling water recovery tank and/or a warm water tank and/or a warm water storage tank monitor the liquid level of the tank liquid, the electronically controlled level gauge being communicatively coupled to the control center K, When the control center K receives the liquid level sent by the electronically controlled liquid level gauge lower than the set liquid level, the inflow valve of each tank and the pump open the injection liquid to the set liquid level. Through the control of the electronically controlled hygrometer and the control center K, the fully automatic control of the liquid level of each device in the entire production line is realized.

The water quality of the water treatment wastewater recovery treatment zone of the herbal fiber bioremediation production line and the water quality of the inactivated wastewater recovery treatment zone are monitored in real time by a water quality monitor, and the water quality detector is connected to the control center K for communication. When the center K receives the information that the water quality detector sends the water quality in accordance with the specified indicators, the water can be recycled or discharged into the natural waters. When the control center K receives the water quality from the water quality detector, the water quality exceeds the specified index. An alert message is issued. Through the control of the electronically controlled hygrometer and the control center K, the fully automatic control of the liquid level of each device in the entire production line is realized.

Monitoring the harmful substance concentration of the integrated exhaust gas discharge port of the herb fiber bio-refining production line by a harmful gas monitor, and the harmful gas monitor is connected with the control center K, and when the gas meets the set index, it can be discharged to In the atmosphere, when the control center K receives the information that the concentration of harmful substances from the harmful gas monitor exceeds the set index, an alarm message is issued.

The exhaust gas discharged from the integrated exhaust gas discharge port comprises a hot gas and/or a fermentation device S3 and/or an emulsified oil blending tank and/or an emulsified oil recovery tank formed by the opening device S8 through the exhaust fan to cool the material and/or Emulsified oil storage tank and/or tap water storage tank G5 and/or clean water recovery tank G6 and/or hot water recovery tank G7 and/or hot water storage tank G8 and/or cooling water recovery tank G9 and/or warm water mixing tank G10 And/or warm water storage tank G11 and/or bacterial suspension mixing tank G12 and/or water treatment waste recovery treatment area and/or inactivated waste liquid recovery treatment area Q1 and/or waste residue recovery treatment area and/or strain preparation The gas emitted by J.

The following is the internal monitoring method of the herbal fiber biorefining automatic production line of the present invention for each device:

In the present invention, the tissue type non-cellulosic material produced by mechanical peeling during the processing of the material by the particle extractor discharge pretreatment apparatus S1 can also be controlled by the control center K. In order to prevent the accumulation of excessively organized non-cellulosic materials, the pretreatment unit cannot operate normally or enter the next process to affect the quality of the end product.

The first flow control valve and the first liquid booster pump for supplying warm water to the inoculating device S2 are controlled by the control center K, thereby controlling the ratio of the bacterial liquid to the warm water to sufficiently mix the two to form a bacterial suspension, and passing through the control center K Controlling the second liquid boosting pump and the second flow control valve to control the bacterial suspension to be input to the bacterial liquid spraying device of the inoculating device S2 according to the set amount, and the bacterial liquid spraying device is under the control of the control center K Spray the bacterial suspension onto the material. Through the scheme, the automatic suspension of the bacterial suspension according to the set ratio and the quantitative automatic spraying of the bacterial liquid spraying device are realized, thereby realizing more precise control of the suspension of the suspension of the bacteria.

An air supply flow control valve for supplying steam into the closed casing of the fermentation device S3, a water supply flow control valve for supplying water to the closed casing, and an atomizing device connected to the water supply flow control valve by the control center K, the fermentation device S3 further includes a thermometer and a hygrometer located in the housing and respectively communicating with the control center K, the control center K controlling the air supply flow control valve according to the information transmitted by the thermometer, according to the humidity The information transmitted is controlled to control the water supply flow control valve and the atomizing device. Through this scheme, automatic control of temperature and humidity in the fermentation apparatus S3 is achieved.

The camera at the beginning of the material transport mechanism and the middle and rear segments of the fermentation device S3 can also be used to monitor the process maturity mark of the fermentation product. When the process mature mark appears earlier than the set time, the control center controls the material transfer mechanism of the fermentation device S3, The material conveying mechanism of the inactivation device S4, the material conveying mechanism of the water treatment device S5, the material conveying mechanism of the oiling device S6, the material conveying mechanism of the drying device S7, and the material conveying mechanism of the opening device S8 increase the material conveying speed. When the process maturity sign appears later than the set time, the control center controls the material transport mechanism of the fermentation equipment S3, the material transport mechanism of the inactivation equipment S4, the material transport mechanism of the water treatment equipment S5, the material transport mechanism of the oil staining equipment S6, and the drying The material transfer mechanism of the dry device S7 and the material transfer mechanism of the open device S8 reduce the material transfer speed. When the process maturity flag is restored to occur at the set time, the control center controls the material transfer mechanism of the fermentation device S3, the material transfer mechanism of the inactivation device S4, the material transfer mechanism of the water treatment device S5, the material transfer mechanism of the oil staining device S6, The material conveying mechanism of the drying device S7 and the material conveying mechanism of the opening device S8 restore the originally set speed.

A flow control valve, a liquid transfer pump, and a water spray device that supply hot water to the inactivation device S4 are controlled by the control center K, and the flow control valve and the liquid transfer pump are quantitatively supplied under the control of the control center K The water spray device sprays water onto the material under the control of the control center K, and detects the water quality of the inactivated waste liquid recovery treatment area Q1 after the water treatment by the water quality detector, and the water quality detector communicates with the control center K. After the connection, the control center K receives the information that the water quality of the water quality detector meets the requirements, and then controls the extraction pump to deliver the treated water to the hot water storage tank G8. Through this scheme, automatic control of hot water supply, water spray and recycling is realized, and each link of the hot water circulation is harmoniously connected together.

The temperature in the inactivation device S4 of the shutdown production is detected by a thermometer, and the thermometer is communicatively connected to the control center K, and the control center K controls the internal spray to the inactivation device S4 to increase the temperature according to the information transmitted from the thermometer. The spray device causes the temperature in the inactivation device S4 to reach a set starting temperature.

An outflow flow control valve of the tap water storage tank G5 that supplies water to the water treatment device S5, a liquid booster pump, and a water spray device connected to the outflow flow control valve are controlled by the control center K, and the water spray device is in the Water is sprayed onto the material under the control of the control center K. The water treatment waste liquid flows to the water treatment waste liquid recovery treatment area Q2 for treatment, and the water quality of the water treatment waste liquid recovery treatment area Q2 is detected by the water quality detector, and when the control center K receives the water quality from the water quality monitor When the information of the setting request is reached, the inflow flow control valve and the extraction pump of the clean water recovery tank G6 are controlled to deliver the water that has reached the set requirement to the clean water recovery tank G6. When the liquid level in the hot water recovery tank G7 is lower than the liquid level set by the control center, the control center K controls the inflow flow control valve of the hot water recovery tank G7 to deliver the water that has reached the set requirement to the hot water recovery tank G7. Through this program, the automatic control of water supply, water spray, water quality monitoring and recycling of water treatment equipment S5 is realized.

Controlling the first flow control valve of the emulsified oil storage tank G4 of the oil slick device S6, the effluent liquid boosting pump and the fuel injection device connected to the first flow control valve through the control center K, the fuel injection device is in the control center Under the control of K, the emulsified oil is sprayed on the material, and the first extraction pump is controlled by the control center K to transport the oil waste liquid to the emulsified oil recovery tank G2 through the one-way control valve, and then the second pump is controlled by the control center K. The pump and the second flow control valve transport the oil waste liquid in the emulsion recovery tank to the first emulsified oil mixing tank G3, and control the third priming pump and the third flow control valve to control the first emulsification through the control center K. The oil stock solution Y1 and the oil-repellent waste liquid are thoroughly mixed according to a set ratio, and the mixed oil is heated to a set temperature by the steam flowing through the steam flow control valve controlled by the control center K, and then, The fourth extraction pump and the fourth flow control valve controlled by the control center K are sent to the emulsified oil storage tank G4 for recycling. Through this scheme, the automatic control of oil supply, fuel injection, heating and recycling of S6 equipment of oil-staining equipment is realized.

The temperature in the oil repellent equipment S6 of the shutdown production is detected by a thermometer, and the thermometer is communicatively connected with the control center K, and the control center K controls the spray device for spraying the interior of the oil slicking device S6 to increase the temperature according to the information transmitted from the thermometer. So that the temperature in the oil slicker S6 reaches the set starting temperature.

A flow control valve for supplying steam to the heat exchanger of the drying device S7 and a gas trap, a pump and a one-way control valve for recovering steam condensed water in the heat exchanger are controlled by the control center K, and the steam condensed water passes through the gas The trap, the pump and the one-way control valve are recovered to the emulsified oil recovery tank G2, and the air blower connected to the drying device S7 is controlled by the control center K to extract the water formed by the evaporation of the water in the drying device S7. The steam is recovered to the hot water recovery tank G7 via a one-way control valve. Through this scheme, the automatic control of steam supply and recovery in the drying equipment S7 is realized.

The demineralized water extraction pump and the softened water flow control valve for supplying the softened water to the second emulsified oil blending tank G1 of the opening device S8 are controlled by the control center K, and the second emulsified oil blending tank G1 is also received at the high position and Flowing through the second emulsified oil stock solution Y2 of the extraction pump and the flow control valve controlled by the control center K, the second emulsified oil stock solution Y2 and the softened water are thoroughly mixed according to the set ratio, and the oil flow control valve is controlled by the control center K The oil liquid booster pump and the fuel injection device uniformly spray the rated amount of the emulsified oil onto the material, and the exhaust fan connected to the inside of the opening device S8 is controlled by the control center K to discharge the material cooling device in the opening device S8. The hot gas formed is discharged to the outside of the opening device S8 via a one-way control valve. Through the scheme, the emulsified oil supply of the opening device S8 and the automatic control of the hot gas discharge generated by the drying are realized.

The first flow control valve is controlled by the control center K, so that the cooling water from the strain preparation room J and having a certain output pressure flows into the cooling water recovery tank G9, and the cooling water from the strain preparation room J and having a certain output pressure is the bacteria. The water after the heat exchange of the preparation room J. The water in the cooling water recovery tank G9 is sent to the tap water storage tank G5 when the cooling water recovery tank G9 is full, and a one-way control valve is provided between the cooling water recovery tank G9 and the tap water storage tank G5. The high water of the tap water storage tank is returned to the cooling water recovery tank G9 or returned to the strain preparation room J where the cooling water output pressure is lost. Through the scheme, the supply of cold water and hot water in the preparation room of the strain and the automatic control of the recycling of the water and waste liquid are realized.

The above embodiments are merely exemplary embodiments of the present invention, and are not intended to limit the invention, and the scope of the invention is defined by the claims. It is also within the scope of the present invention to make various modifications or equivalents to the present invention within the spirit and scope of the invention.

Claims

The invention discloses a whole process monitoring method for an automatic production line of herbal fiber bio-refining, which is characterized in that a material conveying mechanism of a pretreatment device, a material conveying mechanism of the inoculating device, a material conveying mechanism of the fermentation device, a material conveying mechanism of the inactivating device, and a Material conveying mechanism of water treatment equipment, material conveying mechanism of oiling equipment, material conveying mechanism of drying equipment, material conveying mechanism of opening equipment, material conveying mechanism of packaging equipment, and material transfer mechanism between adjacent equipment The speed of pre-treatment, inoculation, fermentation, inactivation, water treatment, oiling, drying, opening and packaging is coordinated according to the line speed set by the control center and the seamless connection between adjacent processes is achieved.
The method for monitoring a whole process of an automatic production line of herbal fiber biorefining according to claim 1, wherein the pretreatment device and/or the inoculation device and/or the fermentation device and/or the inactivation device and/or the water treatment are monitored by a camera. Material transfer status of the equipment and/or the oiling equipment and/or the drying equipment and/or the opening equipment, when the control center receives the fault signal sent by the camera, a forced braking command is issued to control each device to automatically stop running. .
The method for monitoring the entire process of the automatic production line of the herb fiber biorefining according to claim 2, wherein the camera at the starting end of the material conveying mechanism of the fermentation device and the middle and rear segments thereof can also be used for monitoring the process mature mark of the fermentation product, when the process The maturity sign appears earlier than the set time. The control center controls the material transport mechanism of the fermentation equipment, the material transport mechanism of the inactivation equipment, the material transport mechanism of the water treatment equipment, the material transport mechanism of the oil staining equipment, and the material transport mechanism of the drying equipment. And the material transfer mechanism of the opening device increases the material transfer speed; when the process mature mark appears later than the set time, the control center controls the material transfer mechanism of the fermentation device, the material transfer mechanism of the inactivation device, the material transfer mechanism of the water treatment device, The material conveying mechanism of the oiling equipment, the material conveying mechanism of the drying equipment and the material conveying mechanism of the opening equipment reduce the material conveying speed; when the process mature sign is restored to occur at the set time, the control center controls the material conveying mechanism of the fermentation equipment, Material transfer mechanism, water for inactivating equipment The material conveying mechanism of the equipment, the material conveying mechanism of the oiling equipment, the material conveying mechanism of the drying equipment, and the material conveying mechanism of the opening equipment restore the originally set speed.
The method for monitoring the entire process of the automatic production line of herbal fiber biorefining according to claim 1, wherein the control unit controls the liquid spray device of the inoculation device, the steam supply device of the fermentation device, the hot water supply device of the inactivation device, The cold water supply device of the water treatment equipment and the fuel injection device of the oil pollution equipment supply the bacterial liquid, steam, hot water, cold water and emulsified oil according to the amount set by the control center.
The method according to claim 1, wherein the electronically controlled thermometer is communicatively coupled to the control center, and the temperature of the inoculation device is controlled by an electronically controlled thermometer and/or The amount of warm water spray of the fermentation equipment and/or the amount of hot water spray of the inactivation equipment and/or the amount of hot oil spray of the oil slick equipment and/or the steam flow of the drying equipment adjust the starting temperature of the material transfer space of each equipment; Monitoring the fermentation equipment and/or inactivation equipment and/or oiling equipment and/or drying equipment and/or opening equipment and/or emulsified oil blending tanks and/or hot water recovery tanks and/or by electronically controlled thermometers The temperature of the warm water tank is adjusted, when the control center receives the temperature sent by the electronic control thermometer below the set temperature, the open warm water flow control valve is injected to the fermentation equipment to inject warm water and spray and/or issue the open steam flow control. Instructions for injecting steam into the inactivation device and/or the oil staining device and/or the drying device and/or the emulsified oil blending tank and/or the hot water recovery tank and/or the warm water mixing tank, when the control center When the temperature of the electronically controlled thermometer that receives the opening device is higher than the set temperature, an instruction to accelerate the operation of the blower in the device is issued.
The method according to claim 1, wherein the electronically controlled hygrometer is communicably connected to the control center, and the fermentation equipment is monitored and/or dried by an electronically controlled hygrometer. Humidity in the device and/or opening device, controlling the dehumidifying device and/or opening device of the drying device when the control center receives the humidity sent by the electronically controlled hygrometer beyond a set humidity range The dehumidification device accelerates the dehumidification or slows down the dehumidification or stops the dehumidification, and when the control center receives the humidity in the fermentation device sent by the electronically controlled hygrometer, the temperature is lower than the set humidity range, and the warm water flow control valve is opened. The fermentation equipment is filled with warm water and sprayed to maintain the humidity in the fermentation equipment and/or drying equipment and/or the opening equipment within a set range.
The method for monitoring the entire process of the automatic production line of herbal fiber bio-refining according to claim 1, wherein the electronically controlled liquid level meter is connected to the control center, and the herb fiber bio-refining production line is monitored by an electronically controlled liquid level meter. Emulsified oil recovery tank and / or emulsified oil blending tank and / or emulsified oil storage tank and / or tap water storage tank and / or clean water recovery tank and / or hot water recovery tank and / or hot water storage tank and / or cooling water The recovery tank and/or the warm water mixing tank and/or the warm water storage tank monitor the liquid level of the tank liquid, and when the control center receives the liquid level sent by the electric control liquid level gauge, the liquid level is lower than the set liquid level. The inflow valve and pump of the tank open the injected liquid to the set level.
The method for monitoring the entire process of the automatic production line of the herb fiber biorefining according to claim 1, wherein the water quality and the inactivated wastewater recovery treatment area of the wastewater treatment and treatment area of the herb fiber bioremediation production line are monitored in real time by a water quality monitor. The water quality detector is connected to the control center, and the alarm center sends an alarm message when the water quality detector receives the information that the water quality exceeds the specified index.
The method for monitoring the entire process of the automatic production line of the herb fiber biorefining according to claim 1, characterized in that the harmful substance concentration of the integrated exhaust gas discharge port of the herb fiber biorefining production line is monitored by a harmful gas monitor, the harmful gas monitor And communicating with the control center, and sending an alarm message when the control center receives the information that the concentration of harmful substances from the harmful gas monitor exceeds the set index.
The method for monitoring the entire process of the automatic production line of the herb fiber biorefining according to claim 9, wherein the exhaust gas discharged from the integrated exhaust gas discharge port comprises hot gas and/or fermentation formed by the opening device discharging the material through the exhaust fan to cool the material. Equipment and/or emulsified oil blending tanks and/or emulsified oil recovery tanks and/or emulsified oil storage tanks and/or tap water storage tanks and/or clean water recovery tanks and/or hot water recovery tanks and/or hot water storage Tank and/or cooling water recovery tank and/or warm water tank and/or warm water storage tank and/or bacterial suspension tank and/or water treatment waste recovery treatment zone and/or inactivated waste recovery treatment zone and/or Or the gas discharged from the waste residue treatment treatment area and/or the preparation of the strain.
The method for monitoring the entire process of the automatic production line of herbal fiber bio-refining according to claim 1, wherein the control unit controls the particulate non-cellulosic material produced by the mechanical stripping during the processing of the material by the particle extractor.
The method for monitoring the entire process of the automatic production line of herbal fiber biorefining according to claim 1, wherein the first flow control valve and the first liquid boosting pump for supplying warm water to the inoculation device are controlled by the control center, thereby controlling the bacteria The ratio of the liquid to the warm water is such that the two are thoroughly mixed to form a bacterial suspension, and the second liquid boosting pump and the second flow control valve are controlled by the control center to control the bacterial suspension to be injected into the inoculating device according to the set amount. The device, the bacterial spray device sprays the bacterial suspension onto the material under the control of the control center.
The method for monitoring the entire process of the automatic production line of herbal fiber bio-refining according to claim 1, wherein the control center controls the supply flow control valve for supplying steam to the closed casing of the fermentation device, and the water supply flow control for supplying water to the closed casing. a valve and an atomizing device connected to the water supply flow control valve, the fermentation device further comprising a thermometer and a hygrometer located in the housing and respectively communicably connected to the control center, the control center transmitting according to the thermometer The incoming information controls the supply air flow control valve, and controls the water supply flow control valve and the atomization device based on information transmitted from the hygrometer.
The whole process monitoring method for the automatic production line of herbal fiber bio-refining according to claim 13, characterized in that the camera at the starting end of the material conveying mechanism and the middle and rear sections of the fermentation device can also be used for monitoring the process mature mark of the fermentation product, when the process The maturity sign appears earlier than the set time. The control center controls the material transport mechanism of the fermentation equipment, the material transport mechanism of the inactivation equipment, the material transport mechanism of the water treatment equipment, the material transport mechanism of the oil staining equipment, and the material transport mechanism of the drying equipment. And the material conveying mechanism of the opening device increases the plastic conveying speed; when the process mature sign appears later than the set time, the control center controls the material conveying mechanism of the fermentation equipment, the material conveying mechanism of the inactivation equipment, the material conveying mechanism of the water treatment equipment, The material conveying mechanism of the oiling equipment, the material conveying mechanism of the drying equipment and the material conveying mechanism of the opening equipment reduce the material conveying speed; when the process mature sign is restored to occur at the set time, the control center controls the material conveying mechanism of the fermentation equipment, Material transfer mechanism for inactivating equipment, Material handling means of material transport means material processing apparatus of the transmission mechanism, oil stains material transfer mechanism devices, drying devices and opening device to restore the original set speed.
The method for monitoring the entire process of the automatic production line of the herb fiber biorefining according to claim 1, wherein the flow control valve, the liquid transfer pump and the water spray device for supplying hot water to the inactivation device are controlled by the control center. The flow control valve and the liquid transfer pump quantitatively supply hot water under the control of the control center, and the water spray device sprays water to the material under the control of the control center, and detects the inactivated waste liquid recovery treatment by the water quality detector After the water treatment of the water treatment, the water quality detector detects and communicates with the control center. After receiving the information that the water quality of the water quality detector meets the requirements, the control center controls the extraction pump to deliver the treated water to the hot water storage tank.
The method for monitoring the entire process of the automatic production line of the herb fiber biorefining according to claim 15, wherein the temperature in the inactivation device of the shutdown production is detected by a thermometer, and the thermometer is communicatively connected with the control center, the control center A spray device that sprays the interior of the inactivation device to increase the temperature is controlled based on the information transmitted from the thermometer to bring the temperature in the inactivation device to a set starting temperature.
The method for monitoring the entire process of the automatic production line of herbal fiber bio-refining according to claim 1, wherein the outlet flow control valve and the liquid of the tap water storage tank and/or the clean water recovery tank which supply water to the water treatment equipment are controlled by the control center. a booster pump and a water spray device connected to the outflow flow control valve, the water spray device sprays water to the material under the control of the control center; the water treatment waste liquid flows to the water treatment waste liquid recovery treatment area for processing And detecting, by the water quality detector, the water quality of the water treatment waste recovery treatment area, when the control center receives the water quality from the water quality monitor to meet the set requirements and the liquid in the water recovery tank and/or the hot water recovery tank When the information is lower than the liquid level set by the control center, the inflow flow control valve and the extraction pump that control the fresh water recovery tank and/or the hot water recovery tank will deliver the water that meets the set requirements to the clean water recovery tank and/or hot water. Recycling tanks.
The method for monitoring the entire process of the automatic production line of herbal fiber biorefinement according to claim 1, wherein the first flow control valve, the outflow liquid boosting pump and the effluent pump of the emulsified oil storage tank of the oil slick device are controlled by a control center. The fuel injection device connected to the first flow control valve, the fuel injection device sprays the emulsified oil on the material under the control of the control center, and controls the first extraction pump to transport the oil waste liquid through the one-way control valve through the control center Up to the emulsified oil recovery tank, and then controlling the second extraction pump and the second flow control valve through the control center to transport the oil waste liquid in the emulsion recovery tank to the emulsified oil mixing tank, and controlling the third extraction pump through the control center and The third flow control valve controls that the emulsified oil stock solution and the oil-repellent waste liquid are thoroughly mixed according to a set ratio, and the mixed oil is heated to a set temperature by the steam flowing through the steam flow control valve controlled by the control center. Then, the fourth extraction pump and the fourth flow control valve controlled by the control center are sent to the emulsified oil storage tank for recycling.
The method for monitoring the entire process of the automatic production line of the herb fiber biorefining according to claim 18, wherein the temperature in the oil-splatter device for shutdown production is detected by a thermometer, and the thermometer is connected with the control center, and the control center is based on the thermometer. The incoming information controls the spray device that sprays the interior of the oil slicker to raise the temperature so that the temperature within the slicker reaches the set starting temperature.
The method for monitoring the entire process of the automatic production line of herbal fiber biorefining according to claim 1, wherein the flow control valve for supplying steam to the heat exchanger of the drying device and the steam condensing in the heat exchanger are controlled by the control center. Water recovery gas trap, pump and one-way control valve, the steam condensate is recovered to the emulsified oil recovery tank through the gas trap, the pump and the one-way control valve, and the extractor connected to the drying device is controlled by the control center The water vapor formed by the evaporation of the moisture in the material in the drying device is recovered to the hot water recovery tank through the one-way control valve.
The method for monitoring the entire process of the automatic production line of herbal fiber bio-refining according to claim 1, wherein the softened water extraction pump and the softened water flow control for supplying softened water to the emulsified oil blending tank of the opening device are controlled by the control center. The valve and the emulsified oil mixing tank also receive the emulsified oil stock solution flowing through the extraction pump and the flow control valve controlled by the control center, and the emulsified oil stock solution and the softened water are thoroughly mixed according to the set ratio, and the oil flow control valve is controlled through the control center. The oil liquid booster pump and the fuel injection device uniformly spray the rated amount of the emulsified oil onto the material, and control the hot air formed by the cooling of the material in the opening device through the control center to control the exhaust fan communicating with the inside of the opening device. And discharged to the outside of the opening device via a one-way control valve.
The method for monitoring the entire process of the automatic production line of herbal fiber bio-refining according to claim 1, wherein the first flow control valve is controlled by the control center, and the cooling water from the preparation of the strain and having a certain output pressure flows into the cooling water recovery tank. The water in the cooling water recovery tank is sent to the tap water storage tank when the cooling water recovery tank is full, and a one-way control valve is arranged between the cooling water recovery tank and the tap water storage tank to prevent the high level of the tap water storage tank The water is returned to the cooling water recovery tank or back to the strain preparation room where the cooling water output pressure is lost.