Biomass cellulose automatic extraction and energy conversion device based on forestry residues
By designing an automatic extraction and energy conversion device for biomass cellulose from forestry residues and using an automated system for efficient extraction and conversion, the problems of low processing efficiency and resource waste were solved, and the efficient production and environmentally friendly utilization of biomass energy were achieved.
Patent Information
- Application Number
- CN202422592217.8
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-10-26
- Publication Date
- 2025-09-26
- Estimated Expiration
- 2034-10-26
AI Technical Summary
The existing treatment of forestry residues is inefficient and wastes resources seriously, leading to environmental pollution and resource waste problems.
An automatic extraction and energy conversion device for biomass cellulose based on forestry residues is designed, which includes a pretreatment chamber and an enzymatic hydrolysis chamber. A precisely controlled automated system is used to extract and convert biomass cellulose into energy, and efficient extraction is achieved through components such as crushing, filtration, stirring, and pH adjustment.
It achieves efficient utilization of forestry residues, converts waste into valuable biomass energy, improves production efficiency and quality, and is environmentally friendly and economical.
Smart Images

Figure CN223386143U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of energy conversion, in particular to a device for automatic extraction and energy conversion of biomass cellulose based on forestry residues. Background Art
[0002] Forestry residues refer to waste generated during forestry production, forest regeneration, and forest product processing. These wastes include logging residues, forest clearing and tending residues, and wood processing residues. Specifically, forestry residues can be divided into logging residues, including branches, treetops, bark, leaves, roots, vines, and shrubs. Timbering residues refer to offcuts generated during the timbering process. Processing residues include board skin, boards, wood and bamboo offcuts, sawdust, veneer chips, wood cores, shavings, wood blocks, and scraps.
[0003] There are many problems in the treatment of existing forestry residues, such as low treatment efficiency, serious waste of resources and environmental pollution.
[0004] Therefore, how to solve the problems of low processing efficiency and serious waste of resources has become a technical problem that technical personnel in this field urgently need to solve. Utility Model Content
[0005] In view of this, the present invention addresses the deficiencies of the existing technology and proposes an automatic extraction and energy conversion device for biomass cellulose based on forestry residues, aiming to solve the problems of low processing efficiency and serious waste of resources.
[0006] The utility model provides a device for automatic extraction and energy conversion of biomass cellulose based on forestry residues, comprising:
[0007] Pretreatment chamber and enzymatic hydrolysis chamber;
[0008] The pre-treatment chamber comprises:
[0009] A feeding assembly is located on the top of the pretreatment bin;
[0010] A crushing assembly and a filtering assembly, wherein the crushing assembly is located below the feeding assembly, the filtering assembly is located below the crushing assembly, and one side of the filtering assembly is connected to the inner wall of the pre-processing bin, and the other side extends out of the pre-processing bin;
[0011] a liquid outlet assembly, located below the filter assembly, with one side of the liquid outlet assembly extending out of the pre-treatment chamber and the other side of the liquid outlet assembly connected to the inner side wall of the pre-treatment chamber;
[0012] The enzymatic hydrolysis chamber comprises:
[0013] A first stirring assembly is arranged on the top of the enzymatic hydrolysis chamber;
[0014] There are two second stirring components, and the two second stirring components are symmetrically arranged at the bottom of the enzymatic hydrolysis chamber;
[0015] A pH adjustment component is located on the outer wall of the enzymatic hydrolysis chamber and extends into the enzymatic hydrolysis chamber through a liquid inlet pipe;
[0016] There are several temperature sensors, and several of the temperature sensors are located inside the enzymatic hydrolysis chamber.
[0017] Furthermore, the feed assembly comprises:
[0018] A feed hopper is located on the top of the pretreatment bin;
[0019] a screw conveyor, horizontally arranged at the bottom of the feed hopper, one end of the screw conveyor being connected to the feed hopper, and the other end of the screw conveyor extending to the top of the crushing assembly;
[0020] The first motor is arranged on a side of the feed hopper away from the crushing assembly, and the output end of the first motor is connected to the screw conveyor.
[0021] Furthermore, it is characterized in that the crushing component includes:
[0022] A crushing chamber is located in the middle of the pre-treatment chamber, a feed port is provided at the top of the crushing chamber, and the output end of the screw conveyor extends into the feed port;
[0023] The crushing roller is located inside the crushing chamber.
[0024] Furthermore, it is characterized in that the filter assembly includes:
[0025] The screen is located at the bottom of the crushing roller and is arranged obliquely. The high end of the screen is located on the side away from the screw conveyor, and the low end of the screen is provided with a first separation port.
[0026] Furthermore, it is characterized in that the liquid outlet component includes:
[0027] a liquid outlet plate, located at the bottom of the screen, and arranged obliquely, with a high end of the liquid outlet plate located on a side close to the screw conveyor, and a second separation port being arranged at a low end of the liquid outlet plate;
[0028] The liquid collecting tank is located at the bottom of the liquid outlet plate, the liquid collecting tank is connected to the outer side wall of the pretreatment chamber, and a liquid outlet is provided at the bottom of the liquid collecting tank.
[0029] Furthermore, it is characterized in that the top of the enzymatic hydrolysis chamber is connected to the liquid outlet through a liquid inlet pipe, and a liquid inlet valve is provided at one end of the liquid inlet pipe close to the enzymatic hydrolysis chamber.
[0030] Furthermore, it is characterized in that the first stirring component includes:
[0031] A first stirring shaft is vertically arranged at the top of the enzymatic hydrolysis chamber;
[0032] a first stirring blade, comprising a plurality of first stirring blades, the plurality of first stirring blades being staggeredly arranged on the first stirring shaft in a direction perpendicular to the axial direction of the first stirring shaft;
[0033] The second motor is arranged on the inner bottom wall of the enzymatic hydrolysis chamber, and the output end of the second motor is connected to the first stirring shaft.
[0034] Furthermore, the second stirring component includes:
[0035] A second stirring shaft is horizontally arranged at the top of the enzymatic hydrolysis chamber;
[0036] a second stirring blade, comprising a plurality of second stirring blades, the plurality of second stirring blades being staggeredly arranged on the second stirring shaft in a direction perpendicular to the axial direction of the second stirring shaft;
[0037] The third motor is arranged on the inner wall of the enzymatic hydrolysis chamber, and the output end of the third motor is connected to the second stirring shaft.
[0038] Furthermore, it is characterized in that the pH adjustment component includes:
[0039] an acidic storage tank located on the outer wall of the enzymatic hydrolysis chamber, the acidic storage tank being connected to the interior of the enzymatic hydrolysis chamber via a first delivery pipe, and a first valve being provided at one end of the first delivery pipe close to the enzymatic hydrolysis chamber;
[0040] an alkaline storage tank located on the outer wall of the enzymolysis chamber, the alkaline storage tank being connected to the interior of the enzymolysis chamber via a second delivery pipe, and a second valve being provided at one end of the second delivery pipe close to the enzymolysis chamber;
[0041] The pH sensor is arranged inside the enzymatic hydrolysis chamber.
[0042] Furthermore, the automatic extraction and energy conversion device for biomass cellulose based on forestry residues also includes:
[0043] The controller is located on the outer wall of the enzymatic hydrolysis chamber and is connected to the first stirring component, the second stirring component and the pH adjustment component.
[0044] Compared with existing technologies, the present invention offers the following advantages: the automated biomass cellulose extraction and energy conversion device based on forestry residues can efficiently utilize forestry residues, converting waste into valuable biomass energy, which is both environmentally friendly and economical. Through a precisely controlled automated system, continuous biomass cellulose extraction and energy conversion can be achieved, significantly improving the production efficiency and quality of biomass energy. Furthermore, the design of the device takes into account ease of operation and convenient maintenance, making the biomass energy extraction process more efficient, stable, and sustainable. BRIEF DESCRIPTION OF THE DRAWINGS
[0045] Figure 1 This is a schematic diagram of the overall structure of the device for automatic extraction and energy conversion of biomass cellulose from forestry residues according to the present invention;
[0046] Figure 2 This is a schematic diagram of the pretreatment chamber structure of the device for automatic extraction and energy conversion of biomass cellulose from forestry residues according to the present invention;
[0047] Figure 3 This is a schematic diagram of the enzymatic hydrolysis chamber structure of the automatic extraction and energy conversion device of biomass cellulose based on forestry residues in the utility model.
[0048] In the figure: 100, pretreatment chamber; 111, feed hopper; 112, screw conveyor; 113, first motor; 121, crushing chamber; 122, crushing roller; 131, screen; 141, liquid outlet plate; 142, liquid collecting tank; 150, liquid inlet pipe; 151, liquid inlet valve; 200, enzymatic hydrolysis chamber; 210, first stirring component; 211, first stirring shaft; 212, first stirring blade; 213, second motor; 220, second stirring component; 221, second stirring shaft; 222, second stirring blade; 223, third motor; 231, acid storage tank; 232, alkaline storage tank; 240, controller; 250, enzymatic hydrolysis outlet. DETAILED DESCRIPTION
[0049] The following will be combined with the drawings in the embodiments of this application to clearly and completely describe the technical solutions in the embodiments of this application. Obviously, the embodiments described are only part of the embodiments of this application, not all of the embodiments. Based on the embodiments in this application, all other embodiments obtained by ordinary technicians in this field without making creative efforts are within the scope of protection of this application.
[0050] In the description of this application, it should be understood that the terms "center", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside", etc., indicating the orientation or position relationship, are based on the orientation or position relationship shown in the accompanying drawings, and are only for the convenience of describing this application and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be understood as a limitation on this application.
[0051] The terms "first" and "second" are used for descriptive purposes only and should not be construed as indicating or implying relative importance or implicitly specifying the number of the technical features being referred to. Thus, a feature specified as "first" or "second" may explicitly or implicitly include one or more of such features. Throughout this application, unless otherwise specified, "plurality" means two or more.
[0052] In the description of this application, it should be noted that, unless otherwise expressly specified or limited, the terms "mounted," "connected," and "connected" should be understood in a broad sense. For example, they can refer to fixed, detachable, or integral connections; mechanical or electrical connections; direct or indirect connections through an intermediate medium; and internal communication between two components. Those skilled in the art will understand the specific meanings of the above terms in this application based on the specific circumstances.
[0053] See Figure 1-3 As shown, this embodiment provides an automatic extraction and energy conversion device for biomass cellulose based on forestry residues, comprising: a pretreatment chamber 100 and an enzymatic hydrolysis chamber 200; the pretreatment chamber 100 comprises: a feed assembly located at the top of the pretreatment chamber 100; a crushing assembly and a filtering assembly, wherein the crushing assembly is located below the feed assembly, the filtering assembly is located below the crushing assembly, and one side of the filtering assembly is connected to the inner wall of the pretreatment chamber 100, and the other side extends out of the pretreatment chamber 100; a liquid outlet assembly is located below the filtering assembly, one side of the liquid outlet assembly extends out of the pretreatment chamber 100, and the other side of the liquid outlet assembly is connected to the inner wall of the pretreatment chamber 100;
[0054] The enzymatic hydrolysis chamber 200 includes: a first stirring component 210, which is arranged at the top of the enzymatic hydrolysis chamber 200; two second stirring components 220, and the two second stirring components 220 are symmetrically arranged at the bottom of the enzymatic hydrolysis chamber 200; a pH adjustment component, which is located on the outer wall of the enzymatic hydrolysis chamber 200, and the pH adjustment component extends into the interior of the enzymatic hydrolysis chamber 200 through the liquid inlet pipe 150; and a plurality of temperature sensors, and the plurality of temperature sensors are located inside the enzymatic hydrolysis chamber 200.
[0055] It is understandable that the present embodiment includes a pretreatment chamber 100 and an enzymolysis chamber 200, the pretreatment chamber 100 is used to process raw materials, and the enzymolysis chamber 200 is used to perform enzymolysis reaction under specific pH and temperature conditions to extract biomass cellulose. Through the precise control of the first stirring component 210 and the second stirring component 220 by the controller 240, it can be ensured that the raw materials are fully mixed in the enzymolysis chamber 200, thereby improving the extraction efficiency of cellulose. At the same time, the pH adjustment component can automatically adjust the pH value in the enzymolysis chamber 200 according to the feedback information of the pH sensor, ensuring that the enzymolysis reaction is carried out in the optimal acid-base environment. The setting of the temperature sensor can monitor the temperature in the enzymolysis chamber 200 in real time, ensure that the reaction is carried out within a suitable temperature range, and further improve the efficiency of energy conversion and the extraction rate of biomass cellulose.
[0056] It is understandable that the pretreatment chamber 100 and the enzymatic hydrolysis chamber 200 are preferably made of stainless steel or high-performance materials such as polytetrafluoroethylene (PTFE) and glass fiber reinforced plastic (FRP); the stirring component is preferably made of titanium alloy, which has excellent corrosion resistance, especially in strong acid and strong alkali environments; the filtering component is preferably made of stainless steel wire mesh or composite ceramic material, which can provide higher wear resistance and corrosion resistance, and is easy to clean and maintain.
[0057] Specifically, the feeding assembly includes: a feed hopper 111, located at the top of the pretreatment bin 100; a screw conveyor 112, arranged horizontally at the bottom of the feed hopper 111, one end of the screw conveyor 112 is connected to the feed hopper 111, and the other end of the screw conveyor 112 extends to the top of the crushing assembly; a first motor 113, arranged on the side of the feed hopper 111 away from the crushing assembly, and the output end of the first motor 113 is connected to the screw conveyor 112.
[0058] As will be understood, the feed hopper 111 is used to temporarily store forestry residues, while the auger 112 is used to transport the residues from the feed hopper 111 to the pulverization assembly for pulverization. A first motor 113 powers the auger 112, ensuring continuous and stable material delivery to the pulverization assembly. This not only improves material processing efficiency but also ensures the continuity and automation of the entire extraction process.
[0059] Specifically, it is characterized in that the crushing assembly includes: a crushing chamber 121, located in the middle of the pretreatment bin 100, a feed port is provided at the top of the crushing chamber 121, and the output end of the screw conveyor 112 extends into the feed port; a crushing roller 122, located inside the crushing chamber 121.
[0060] It is understood that the crushing roller 122 crushes the forestry residues entering the crushing chamber 121 by rotating at high speed to achieve a desired particle size.
[0061] Specifically, it is characterized in that the filtering component includes: a screen 131, which is located at the bottom of the crushing roller 122, and the screen 131 is set at an angle, the high end of the screen 131 is located on the side away from the screw conveyor 112, and a first separation port is set at the low end of the screen 131.
[0062] It is understood that the function of screen 131 is to separate the pulverized material and ensure that the cellulose suspension is transported to the liquid outlet assembly. The inclined design of screen 131 facilitates the natural flow of the material. At the same time, the configuration of the first separation port allows large solid residues to be discharged smoothly, while the cellulose suspension continues downward into the liquid outlet assembly.
[0063] Specifically, it is characterized in that the liquid outlet component includes: a liquid outlet plate 141, which is located at the bottom of the screen 131, and the liquid outlet plate 141 is arranged at an angle, the high end of the liquid outlet plate 141 is located on the side close to the screw conveyor 112, and a second separation port is provided at the lower end of the liquid outlet plate 141; a liquid collecting tank 142, which is located at the bottom of the liquid outlet plate 141, the liquid collecting tank 142 is connected to the outer wall of the pretreatment chamber 100, and a liquid outlet is provided at the bottom of the liquid collecting tank 142.
[0064] It is understood that the function of the liquid outlet plate 141 is to guide the cellulose suspension to the liquid collection tank 142, while the second separation port ensures that solid residues do not enter the liquid collection tank 142. The cellulose suspension collected in the liquid collection tank 142 is discharged through the liquid outlet port for subsequent energy conversion. This not only improves the separation efficiency of the materials but also ensures a clean and efficient extraction process. This device can achieve efficient utilization of forestry residues and convert waste into valuable biomass energy, which is both environmentally friendly and economical.
[0065] Specifically, it is characterized in that the top of the enzymatic hydrolysis chamber 200 is connected to the liquid outlet through a liquid inlet pipe 150, and a liquid inlet valve 151 is provided at one end of the liquid inlet pipe 150 close to the enzymatic hydrolysis chamber 200.
[0066] It is understood that the combination of the liquid inlet pipe 150 and the liquid inlet valve 151 enables the cellulose suspension extracted from the pretreatment chamber 100 to be precisely controlled and delivered to the enzymatic hydrolysis chamber 200. The setting of the liquid inlet valve 151 allows the operator to adjust the flow rate of the cellulose suspension according to the actual needs of the enzymatic hydrolysis reaction, ensuring that an appropriate liquid cellulose concentration is maintained in the enzymatic hydrolysis chamber 200, thereby optimizing the enzymatic hydrolysis efficiency.
[0067] Specifically, it is characterized in that the first stirring component 210 includes: a first stirring shaft 211, which is arranged at the top of the enzymatic hydrolysis chamber 200 in a vertical direction; a first stirring blade 212, which has a plurality of first stirring blades 212, which are staggered on the first stirring shaft 211 in a direction perpendicular to the axial direction of the first stirring shaft 211; a second motor 213, which is arranged on the inner bottom wall of the enzymatic hydrolysis chamber 200, and the output end of the second motor 213 is connected to the first stirring shaft 211.
[0068] It is understood that the first stirring shaft 211 is rotated by the second motor 213, thereby achieving sufficient stirring of the liquid cellulose in the enzymatic hydrolysis chamber 200. The design of the first stirring blade 212 makes stirring more uniform, which helps to improve the efficiency of the enzymatic hydrolysis reaction and the extraction rate of biomass cellulose. In addition, the provision of the first stirring assembly 210 can also prevent possible material deposition in the enzymatic hydrolysis chamber 200, ensuring the uniformity of the reaction process.
[0069] Specifically, the second stirring assembly 220 includes: a second stirring shaft 221, which is horizontally arranged at the top of the enzymatic hydrolysis chamber 200; a second stirring blade 222, which has a plurality of second stirring blades 222, which are staggered on the second stirring shaft 221 along a direction perpendicular to the axial direction of the second stirring shaft 221; a third motor 223, which is arranged on the inner side wall of the enzymatic hydrolysis chamber 200, and the output end of the third motor 223 is connected to the second stirring shaft 221.
[0070] It is understood that the second stirring shaft 221 is rotated by the drive of the third motor 223 and works in conjunction with the first stirring assembly 210 to further ensure that the liquid cellulose in the enzymatic hydrolysis chamber 200 is evenly mixed. The design of the second stirring blade 222 also helps to improve the stirring efficiency and prevent the material from depositing during the enzymatic hydrolysis process, thereby maintaining the uniformity and continuity of the enzymatic hydrolysis reaction. Through the configuration of this dual stirring assembly, it is possible to achieve fine control of the enzymatic hydrolysis process and ensure that the extraction efficiency of biomass cellulose is maximized.
[0071] Specifically, it is characterized in that the pH adjustment component includes: an acidic storage tank 231, located on the outer wall of the enzymatic hydrolysis chamber 200, the acidic storage tank 231 is connected to the interior of the enzymatic hydrolysis chamber 200 through a first delivery pipe, and a first valve is provided at one end of the first delivery pipe close to the enzymatic hydrolysis chamber 200; an alkaline storage tank 232, located on the outer wall of the enzymatic hydrolysis chamber 200, the alkaline storage tank 232 is connected to the interior of the enzymatic hydrolysis chamber 200 through a second delivery pipe, and a second valve is provided at one end of the second delivery pipe close to the enzymatic hydrolysis chamber 200; a pH sensor is arranged inside the enzymatic hydrolysis chamber 200.
[0072] It is understandable that the pH sensor is used to monitor the pH value in the enzymatic hydrolysis chamber 200 in real time to ensure that the enzymatic hydrolysis process is carried out in a suitable acid-base environment. When it is detected that the pH value deviates from the preset range, the system will automatically adjust the opening and closing of the first valve or the second valve to control the amount of acidic or alkaline substance added to achieve the purpose of quickly adjusting the pH value. This automated pH adjustment mechanism not only improves the stability and reliability of the enzymatic hydrolysis process, but also reduces manual intervention, further improving the efficiency and automation level of the entire biomass energy extraction process.
[0073] Specifically, an enzymolysis outlet 250 is further provided at the bottom of the enzymolysis chamber 200 .
[0074] Specifically, the automatic extraction and energy conversion device of biomass cellulose based on forestry residues also includes: a controller 240, located on the outer wall of the enzymatic hydrolysis chamber 200, and the controller 240 is connected to the first stirring component 210, the second stirring component 220 and the pH adjustment component.
[0075] It is understood that controller 240, as the intelligent core of the entire device, is responsible for receiving data from various components and analyzing and processing this data according to pre-set programs and algorithms. Controller 240 is able to monitor and adjust the operating status of first stirring component 210 and second stirring component 220 in real time to ensure uniformity and efficiency of stirring. Simultaneously, controller 240 works closely with the pH adjustment component, automatically adjusting the addition of acid and base substances based on feedback from the pH sensor to maintain the pH value of the enzymatic hydrolysis process within the optimal range.
[0076] In summary, the automated biocellulose extraction and energy conversion device based on forestry residues provided in this embodiment enables efficient utilization of forestry residues, converting waste into valuable biomass energy, which is both environmentally friendly and economical. Through a precisely controlled automated system, continuous biocellulose extraction and energy conversion can be achieved, significantly improving the production efficiency and quality of biomass energy. Furthermore, the design of this device also takes into account ease of operation and convenient maintenance, making the biomass energy extraction process more efficient, stable, and sustainable.
[0077] Obviously, those skilled in the art may make various modifications and variations to the present invention without departing from the spirit and scope of the present invention. Thus, if such modifications and variations fall within the scope of the claims of the present invention and their equivalents, the present invention is intended to include such modifications and variations.
Claims
1. A device for automatic extraction and energy conversion of biomass cellulose from forestry residues, characterized in that: include: Pretreatment chamber and enzymatic hydrolysis chamber; The pre-treatment chamber comprises: A feeding assembly is located on the top of the pretreatment bin; A crushing assembly and a filtering assembly, wherein the crushing assembly is located below the feeding assembly, the filtering assembly is located below the crushing assembly, and one side of the filtering assembly is connected to the inner wall of the pre-processing bin, and the other side extends out of the pre-processing bin; a liquid outlet assembly, located below the filter assembly, with one side of the liquid outlet assembly extending out of the pre-treatment chamber and the other side of the liquid outlet assembly connected to the inner side wall of the pre-treatment chamber; The enzymatic hydrolysis chamber comprises: A first stirring assembly is arranged on the top of the enzymatic hydrolysis chamber; There are two second stirring components, and the two second stirring components are symmetrically arranged at the bottom of the enzymatic hydrolysis chamber; A pH adjustment component is located on the outer wall of the enzymatic hydrolysis chamber and extends into the enzymatic hydrolysis chamber through a liquid inlet pipe; There are several temperature sensors, and several of the temperature sensors are located inside the enzymatic hydrolysis chamber.
2. The automatic extraction and energy conversion device of biomass cellulose based on forestry residues according to claim 1 is characterized in that: The feed assembly comprises: A feed hopper is located on the top of the pretreatment bin; a screw conveyor, horizontally arranged at the bottom of the feed hopper, one end of the screw conveyor being connected to the feed hopper, and the other end of the screw conveyor extending to the top of the crushing assembly; The first motor is arranged on a side of the feed hopper away from the crushing assembly, and the output end of the first motor is connected to the screw conveyor.
3. The automatic extraction and energy conversion device of biomass cellulose based on forestry residues according to claim 2 is characterized in that: The crushing assembly includes: A crushing chamber is located in the middle of the pre-treatment chamber, a feed port is provided at the top of the crushing chamber, and the output end of the screw conveyor extends into the feed port; The crushing roller is located inside the crushing chamber.
4. The automatic extraction and energy conversion device of biomass cellulose based on forestry residues according to claim 3 is characterized in that: The filter assembly comprises: The screen is located at the bottom of the crushing roller and is arranged obliquely. The high end of the screen is located on the side away from the screw conveyor, and the low end of the screen is provided with a first separation port.
5. The automatic extraction and energy conversion device of biomass cellulose based on forestry residues according to claim 4 is characterized in that: The liquid outlet component comprises: a liquid outlet plate, located at the bottom of the screen, and arranged obliquely, with a high end of the liquid outlet plate located on a side close to the screw conveyor, and a second separation port being arranged at a low end of the liquid outlet plate; The liquid collecting tank is located at the bottom of the liquid outlet plate, the liquid collecting tank is connected to the outer side wall of the pretreatment chamber, and a liquid outlet is provided at the bottom of the liquid collecting tank.
6. The automatic extraction and energy conversion device of biomass cellulose based on forestry residues according to claim 5 is characterized in that: The top of the enzymolysis chamber is connected to the liquid outlet through a liquid inlet pipe, and a liquid inlet valve is provided at one end of the liquid inlet pipe close to the enzymolysis chamber.
7. The automatic extraction and energy conversion device of biomass cellulose based on forestry residues according to claim 1 is characterized in that: The first stirring component comprises: A first stirring shaft is vertically arranged at the top of the enzymatic hydrolysis chamber; a first stirring blade, comprising a plurality of first stirring blades, the plurality of first stirring blades being staggeredly arranged on the first stirring shaft in a direction perpendicular to the axial direction of the first stirring shaft; The second motor is arranged on the inner bottom wall of the enzymatic hydrolysis chamber, and the output end of the second motor is connected to the first stirring shaft.
8. The automatic extraction and energy conversion device of biomass cellulose based on forestry residues according to claim 1 is characterized in that: The second stirring component includes: A second stirring shaft is horizontally arranged at the top of the enzymatic hydrolysis chamber; a second stirring blade, comprising a plurality of second stirring blades, the plurality of second stirring blades being staggeredly arranged on the second stirring shaft in a direction perpendicular to the axial direction of the second stirring shaft; The third motor is arranged on the inner wall of the enzymatic hydrolysis chamber, and the output end of the third motor is connected to the second stirring shaft.
9. The automatic extraction and energy conversion device of biomass cellulose based on forestry residues according to claim 1 is characterized in that: The pH adjustment component includes: an acidic storage tank located on the outer wall of the enzymatic hydrolysis chamber, the acidic storage tank being connected to the interior of the enzymatic hydrolysis chamber via a first delivery pipe, and a first valve being provided at one end of the first delivery pipe close to the enzymatic hydrolysis chamber; an alkaline storage tank located on the outer wall of the enzymolysis chamber, the alkaline storage tank being connected to the interior of the enzymolysis chamber via a second delivery pipe, and a second valve being provided at one end of the second delivery pipe close to the enzymolysis chamber; The pH sensor is arranged inside the enzymatic hydrolysis chamber.
10. The automatic extraction and energy conversion device of biomass cellulose based on forestry residues according to claim 1, characterized in that: The automatic extraction and energy conversion device for biomass cellulose based on forestry residues also includes: The controller is located on the outer wall of the enzymatic hydrolysis chamber and is connected to the first stirring component, the second stirring component and the pH adjustment component.