Assembly line separation preparation system for preparing fiber and extract by using mulberry branches
The automated separation and preparation system processes mulberry branches through soaking, heating and steaming, and peeling, solving the problems of difficult wastewater treatment and high energy consumption in the utilization of mulberry branches. This achieves efficient resource utilization and product quality improvement of mulberry branches, reduces environmental pollution, and provides raw materials for multiple industries.
Patent Information
- Application Number
- CN202423111161.6
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-12-17
- Publication Date
- 2025-10-31
- Estimated Expiration
- 2034-12-17
AI Technical Summary
Existing methods for utilizing mulberry branches suffer from problems such as difficulty in wastewater treatment, high energy consumption, poor product quality, high wastewater treatment costs, and underutilization of resources. Furthermore, the production process involves environmental pollution caused by the open burning of raw materials.
A streamlined separation and preparation system was designed, including a cutting machine, a cooking pot, a peeling machine, a surface black bark separator, a microwave dryer, a carding machine, a storage tank, a membrane concentration treatment device, and a vacuum concentrator. Through processes such as soaking, heating and cooking, peeling, microwave drying, and membrane concentration, bast fibers, stalk fibers, and mulberry branch extract products are separated, realizing the comprehensive extraction of mulberry branches and the efficient utilization of resources.
It has achieved efficient decomposition of mulberry branches and full utilization of resources, improved product conversion rate, reduced production costs, provided raw materials for multiple industries, reduced environmental pollution, increased farmers' income, and improved the ecological environment.
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Figure CN223496915U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of mulberry branch extraction technology, and in particular to a streamlined separation and preparation system for preparing fibers and extracts from mulberry branches. Background Technology
[0002] Mulberry trees have a wide range of uses, serving as both a high-quality fiber raw material and a traditional Chinese medicinal herb. However, the scientific utilization of mulberry branches is a major technological challenge. Existing methods for utilizing mulberry branches suffer from several problems: the water separated after cooking the dry branches is not effectively utilized, leading to difficult wastewater treatment; enzymatic hydrolysis processes are time-consuming and energy-intensive in processing both cooked and wet mulberry branches; and pulping with bast and stems results in numerous black spots and poor quality, making them unsuitable for large-scale industrial production. Furthermore, in practice, even when the bark and stem are completely separated during the bark-stem separation process, excessive degumming can still occur, damaging the bast fiber structure. The bark, husk, and bast are not completely separated and remain intertwined; even the separated bark and husk contain traces of bast, making it difficult to remove these components in subsequent processes. Pulping methods using biological processes, APMP, or extrusion machinery often produce products with numerous small black bark and husk particles, failing to meet quality requirements and resulting in products that are not accepted by the market. Meanwhile, the pulping process using bast bark and stems results in the release of large amounts of pectin and crude protein solutions into the wastewater. Furthermore, APMP or extrusion pulping wastewater contains various chemical components, increasing the difficulty and cost of wastewater treatment. The utilization of mulberry branches has become an urgent issue. Researching and developing the utilization of mulberry branches can not only make use of waste mulberry branch resources, but also increase the income of local people, alleviate poverty in impoverished areas, and improve the ecological environment, thus yielding significant social, economic, and environmental benefits. Utility Model Content
[0003] To address the shortcomings of existing technologies, the purpose of this invention is to provide a streamlined separation and preparation system for preparing fibers and extracts from mulberry branches. This system extracts bast fibers, stalk fibers, and mulberry branch extract products from mulberry branches, fully decomposing the useful substances in the branches. This provides raw materials for industries such as pulp and paper making, food, and medicine, increasing income for mulberry agriculture and effectively preventing the open burning of raw materials from polluting the air and causing severe smog.
[0004] The objective of this utility model is achieved through the following technical solution:
[0005] A streamlined separation and preparation system for producing fibers and extracts from mulberry branches includes a cutting machine, a cooking pot, a peeling machine, a surface black bark separator, a microwave dryer, a carding machine, a storage tank, a membrane concentration device, and a vacuum concentrator. The cutting machine has an inlet for cutting mulberry branches into mulberry branch segments. The outlet of the cutting machine is connected to the inlet of the cooking pot, which is used to soak, heat, and cook the mulberry branch segments to separate the cooking liquid from the cooked stem material. The cooking pot has a cooking liquid outlet and a cooked stem material outlet. The cooking liquid outlet of the cooking pot is connected to the inlet of the storage tank via pipe A. The cooked stem material outlet of the cooking pot is connected to the inlet of the peeling machine. The peeling machine is used to peel the cooked stem material to obtain bark material and core stem material. The peeling machine has a bark material outlet and a stem material outlet. The bark peeler's stalk outlet is used to discharge the core stalk material, and the bark outlet is connected to the feed end of the surface black bark separator. The surface black bark separator is used to separate the bark material into surface black bark and bast bark. The surface black bark separator has a bark outlet and a bast bark outlet. The bast bark outlet of the surface black bark separator is connected to the feed inlet of the microwave dryer. The microwave dryer is used to microwave dry the bast bark. The outlet of the microwave dryer is connected to the feed inlet of the carding machine. The carding machine is used to break up and remove impurities from the bast bark to obtain bast bark fibers. The outlet of the storage tank is connected to the inlet of the membrane concentration treatment device through pipe B. The membrane concentration treatment device is used to perform membrane concentration separation treatment on the decoction to obtain concentrated liquid and transport it to the vacuum concentrator. The vacuum concentrator is used to concentrate the concentrated liquid to obtain mulberry branch extract product.
[0006] To better realize this utility model, it also includes a shredder, an enzymatic hydrolysis chamber, a milling machine, and a filter press. The rod material outlet of the peeling machine is connected to the feed inlet of the shredder, which is used to shred the core rod material into fine filaments. The discharge outlet of the shredder is connected to the feed inlet of the enzymatic hydrolysis chamber, which is used to add xylanase to the fine filaments for enzymatic hydrolysis. The discharge outlet of the enzymatic hydrolysis chamber is connected to the feed end of the milling machine, which is used to mill the enzymatically hydrolyzed fine filaments to obtain coarse slurry. The discharge end of the milling machine is connected to the feed end of the filter press, which is used to separate the coarse slurry and filtrate. The coarse slurry is dried to obtain rod fibers.
[0007] Preferably, the present invention further includes a clear liquid tank, a concentrated liquid pool is provided between the membrane concentration treatment device and the vacuum concentrator, the membrane concentration treatment device has a concentrated liquid outlet, the concentrated liquid outlet of the membrane concentration treatment device is connected to the liquid inlet of the concentrated liquid pool through a pipe C, the concentrated liquid pool is used for settling treatment of the concentrated liquid, the concentrated liquid pool has a concentrated liquid outlet, the concentrated liquid outlet of the concentrated liquid pool is connected to the feed end of the vacuum concentrator through a pipe D, and a pump D is installed on the pipe D; the liquid outlet of the clear liquid tank is connected to the cooking pot through a pipe E, and a pump B is installed on the pipe E.
[0008] Preferably, the vacuum concentrator is connected to a condensate tank, and the condensate tank is connected to the clear liquid tank via a pipe F, on which a pump C is installed.
[0009] Preferably, the present invention further includes a filtrate tank, the filter press has a filtrate outlet for discharging filtrate, the filtrate outlet of the filter press is connected to the filtrate tank, the outlet of the filtrate tank is connected to a storage tank via a pipe G, and a pump E is installed on the pipe G.
[0010] Preferably, the discharge port of the cutting machine is connected to the inlet of the cooking pot via a belt conveyor; the cooking material outlet of the cooking pot is connected to the inlet of the peeling machine via a belt conveyor; the peel material outlet of the peeling machine is connected to the inlet of the surface black skin separator via a belt conveyor; and the bast skin outlet of the surface black skin separator is connected to the inlet of the microwave dryer via a belt conveyor.
[0011] Preferably, the present invention also includes a dryer, wherein the skin outlet of the surface black skin separator is connected to the feed end of the dryer via a belt conveyor, and the dryer is used to dry the surface black skin.
[0012] Preferably, the rod outlet of the peeling machine is connected to the feed inlet of the shredder via a belt conveyor; the discharge outlet of the shredder is connected to the feed inlet of the enzymatic hydrolysis chamber via a belt conveyor; and the discharge outlet of the enzymatic hydrolysis chamber is connected to the feed inlet of the grinder via a screw conveyor.
[0013] Preferably, a pump A is installed on the pipe A between the decoction outlet of the decoction pot and the inlet of the storage tank.
[0014] Preferably, a defoaming tank for defoaming treatment of fine filamentous coarse materials is provided between the mill and the filter press.
[0015] Compared with the prior art, this utility model has the following advantages and beneficial effects:
[0016] (1) The production line preparation system of this utility model uses mulberry branches to extract bast fiber, stem fiber and mulberry branch extract products. It can fully decompose the useful substances in mulberry branches, provide raw materials for the pulp and paper industry, food industry, medical industry and other industries, increase income for mulberry agriculture, and effectively avoid the pollution of air caused by open burning of raw materials, which would lead to serious smog.
[0017] (2) This utility model adopts cross-industry development and utilization and fully utilizes and transforms mulberry branch resources, realizing the comprehensive extraction of mulberry branches. Bast fiber and stem fiber can be used in the papermaking industry, mulberry branch extract products can be used in the pharmaceutical or food industry, the separated surface black bark can be recycled and used as raw material for producing mosquito coils or as organic fertilizer, and other waste residues can be used as raw material for producing edible fungi.
[0018] (3) The mulberry branches of this utility model are soaked and heated in a decoction pot to obtain decoction and decoction material. The decoction is further processed to obtain mulberry branch extract product. The decoction material is separated into bark and core material. The bark is then separated from the outer black bark and bast bark. The bast bark is dried by microwave, dispersed and impurity removed to obtain bast fiber. The core material is then torn, enzymatically hydrolyzed, ground and filtered to obtain stem fiber. In this way, the conversion rate and yield of mulberry branch raw materials are significantly improved, and the industrial production cost is reduced. Attached Figure Description
[0019] Figure 1 This is a structural block diagram of an embodiment of the present utility model. Detailed Implementation
[0020] The present invention will be further described in detail below with reference to the embodiments:
[0021] Example
[0022] like Figure 1As shown, a production line separation and preparation system for preparing fibers and extracts using mulberry branches includes a cutting machine, a cooking pot, a peeling machine, a surface black bark separator, a microwave dryer, a carding machine, a storage tank, a membrane concentration treatment device, and a vacuum concentrator. The cutting machine has a feed inlet and is used to cut mulberry branches into 60-80 mm sections (a screening machine can be added after the cutting machine, with a set screening size; in this embodiment, the screening machine is used to remove mulberry branches smaller than 10 mm, while branches between 10-60 mm can be retained). The discharge port of the cutting machine is connected to the feed inlet of the cooking pot, and the discharge port of the cutting machine and the feed inlet of the cooking pot are connected by a belt conveyor. The belt conveyor transports the mulberry branches from the discharge port of the cutting machine to the cooking pot for soaking, heating, and cooking treatment. The decoction pot is used to soak, heat, and cook mulberry branches to separate them into a decoction liquid and a decoction material. The decoction pot has a decoction liquid outlet and a decoction material outlet. The decoction liquid outlet of the decoction pot is connected to the inlet of a storage tank via pipe A. Preferably, a pump A is installed on pipe A between the decoction liquid outlet of the decoction pot and the inlet of the storage tank (pump A provides power for the decoction liquid transport, pumping the decoction liquid from the decoction liquid outlet of the decoction pot to the storage tank). The decoction material outlet of the decoction pot is connected to the feed end of a peeling machine, and a belt conveyor connects the decoction material outlet of the decoction pot to the feed end of the peeling machine; the belt conveyor transports the decoction material from the decoction material outlet of the decoction pot to the peeling machine. The peeling machine is used to peel the stems from boiling materials to obtain the peel material and the core stem material. The peeling machine has a peel material outlet and a stem material outlet. The stem material outlet of the peeling machine is used to discharge the core stem material. The peel material outlet of the peeling machine is connected to the feed end of the surface black skin separator. The peel material outlet of the peeling machine and the feed end of the surface black skin separator are connected by a belt conveyor. The belt conveyor is used to transport the peel material from the peel material outlet of the peeling machine to the surface black skin separator.
[0023] like Figure 1 As shown, the surface black skin separator is used to separate the hide into surface black skin and bast skin. The surface black skin separator has a skin outlet and a bast skin outlet. The bast skin outlet of the surface black skin separator is connected to the inlet of a microwave dryer. Preferably, the bast skin outlet of the surface black skin separator and the inlet of the microwave dryer are connected by a belt conveyor, which transports the bast skin from the bast skin outlet of the surface black skin separator to the microwave dryer. The microwave dryer is used to microwave dry the bast skin. The outlet of the microwave dryer is connected to the inlet of a carding machine, which is used to break up and remove impurities from the bast skin to obtain bast skin fibers.
[0024] like Figure 1As shown, the outlet of the storage tank is connected to the inlet of the membrane concentration treatment device through pipe B. The membrane concentration treatment device is used to perform membrane concentration separation treatment on the decoction to obtain a concentrated liquid, which is then transported to the vacuum concentrator. The vacuum concentrator is used to further concentrate the concentrated liquid to obtain mulberry twig extract (also known as mulberry twig extract or mulberry twig concentrate), which can be used as a raw material for traditional Chinese medicine for further extraction, or as a raw material for the food industry, such as for further extraction of pectin paste.
[0025] In some embodiments, such as Figure 1 As shown, this utility model also includes a shredder, an enzymatic hydrolysis chamber, a mill, and a filter press. The rod material outlet of the peeling machine is connected to the feed inlet of the shredder, and a belt conveyor connects the rod material outlet of the peeling machine to the feed inlet of the shredder. The belt conveyor transports the core rod material from the rod material outlet of the peeling machine to the shredder. The shredder is used to shred the core rod material into fine filaments. The discharge outlet of the shredder is connected to the feed inlet of the enzymatic hydrolysis chamber, and a belt conveyor connects the discharge outlet of the shredder to the feed inlet of the enzymatic hydrolysis chamber. The belt conveyor transports the fine filaments from the discharge outlet of the shredder to the enzymatic hydrolysis chamber. The enzymatic hydrolysis chamber is used to add xylanase to the fine filaments for enzymatic hydrolysis. The discharge outlet of the enzymatic hydrolysis chamber is connected to the feed end of the mill, and a screw conveyor connects the discharge outlet of the enzymatic hydrolysis chamber to the feed end of the mill. The screw conveyor transports the enzymatically hydrolyzed fine filaments from the discharge outlet of the enzymatic hydrolysis chamber to the mill. A grinding mill is used to grind the enzymatically hydrolyzed fine filamentous coarse material to obtain coarse pulp. The discharge end of the grinding mill is connected to the feed end of a filter press, which is used to separate the coarse pulp and filtrate. After drying, the coarse pulp yields rod fibers. Preferably, a de-flaking tank (using a pulping tank suitable for pulp de-flaking treatment) is also provided between the grinding mill and the filter press for de-flaking the fine filamentous coarse material (the purpose of de-flaking is to leach out useful substances from the fibers and also to improve fiber strength). The rod fibers and bast fibers obtained in this embodiment can be used as pulp raw materials in the papermaking industry, which helps reduce the papermaking industry's dependence on trees, reduces deforestation, and helps increase the national forest coverage rate.
[0026] In some embodiments, such as Figure 1 As shown, this utility model also includes a clear liquid tank, a concentrate tank is provided between the membrane concentration treatment device and the vacuum concentrator, the membrane concentration treatment device has a concentrate outlet, the concentrate outlet of the membrane concentration treatment device is connected to the inlet of the concentrate tank through pipe C, the concentrate tank is used for settling treatment of the concentrate, the concentrate tank has a concentrate outlet, the concentrate outlet of the concentrate tank is connected to the feed end of the vacuum concentrator through pipe D, and a pump D is installed on pipe D; the outlet of the clear liquid tank is connected to the cooking pot through pipe E, and a pump B is installed on pipe E. Preferably, the vacuum concentrator is connected to a condensate tank, the condensate tank and the clear liquid tank are connected through pipe F, and a pump C is installed on pipe F.
[0027] In some embodiments, such as Figure 1 As shown, the present invention also includes a filtrate tank, and the filter press has a filtrate outlet for discharging filtrate. The filtrate outlet of the filter press is connected to the filtrate tank, and the outlet of the filtrate tank is connected to the storage tank through a pipe G. A pump E is installed on the pipe G.
[0028] In some embodiments, such as Figure 1 As shown, this utility model also includes a dryer. The skin outlet of the surface black skin separator is connected to the feed end of the dryer via a belt conveyor. The dryer is used to dry the surface black skin.
[0029] The above are merely preferred embodiments of the present utility model and are not intended to limit the present utility model. Any modifications, equivalent substitutions, and improvements made within the spirit and principles of the present utility model should be included within the protection scope of the present utility model.
Claims
1. A streamlined separation and preparation system for preparing fibers and extracts from mulberry branches, comprising a cutting machine, a boiling pot, a peeling machine, a surface black bark separator, a microwave dryer, and a carding machine, characterized in that: It also includes a storage tank, a membrane concentration treatment device, and a vacuum concentrator. The cutting machine has a feed inlet and is used to cut mulberry branches into mulberry twig sections. The discharge port of the cutting machine is connected to the feed inlet of the decoction pot. The decoction pot is used to soak, heat, and cook the mulberry twig sections to separate the decoction liquid and the cooked stem material. The decoction pot has a decoction liquid outlet and a cooked stem material outlet. The decoction liquid outlet of the decoction pot is connected to the inlet of the storage tank through pipe A. The cooked stem material outlet of the decoction pot is connected to the feed end of the peeling machine. The peeling machine is used to peel the cooked stem material to obtain the bark and core stem material. The peeling machine has a bark outlet and a stem material outlet. The stem material outlet of the peeling machine is used to discharge the core stem material. The bark material outlet of the peeling machine is connected to the surface black... The feed end of the skin separator is connected; the surface black skin separator is used to separate the skin into surface black skin and bast skin. The surface black skin separator has a skin outlet and a bast skin outlet. The bast skin outlet of the surface black skin separator is connected to the feed inlet of the microwave dryer; the microwave dryer is used to microwave dry the bast skin. The discharge outlet of the microwave dryer is connected to the feed inlet of the carding machine. The carding machine is used to break up and remove impurities from the bast skin to obtain bast skin fibers; the discharge outlet of the storage tank is connected to the discharge inlet of the membrane concentration treatment device through pipe B. The membrane concentration treatment device is used to perform membrane concentration separation treatment on the decoction to obtain concentrated liquid and transport it to the vacuum concentrator. The vacuum concentrator is used to concentrate the concentrated liquid to obtain mulberry branch extract product.
2. The automated separation and preparation system for preparing fibers and extracts from mulberry branches according to claim 1, characterized in that: It also includes a shredder, an enzymatic hydrolysis chamber, a mill, and a filter press. The rod material outlet of the peeling machine is connected to the feed inlet of the shredder, which is used to shred the core rod material into fine filaments. The discharge outlet of the shredder is connected to the feed inlet of the enzymatic hydrolysis chamber, which is used to add xylanase to the fine filaments for enzymatic hydrolysis. The discharge outlet of the enzymatic hydrolysis chamber is connected to the feed end of the mill, which is used to mill the enzymatically hydrolyzed fine filaments to obtain coarse slurry. The discharge end of the mill is connected to the feed end of the filter press, which is used to separate the coarse slurry and filtrate. The coarse slurry is dried to obtain rod fibers.
3. The automated separation and preparation system for preparing fibers and extracts from mulberry branches according to claim 1, characterized in that: It also includes a clear liquid tank, a concentrate pool is provided between the membrane concentration treatment device and the vacuum concentrator, the membrane concentration treatment device has a concentrate outlet, the concentrate outlet of the membrane concentration treatment device is connected to the inlet of the concentrate pool through pipe C, the concentrate pool is used for settling treatment of the concentrate, the concentrate pool has a concentrate outlet, the concentrate outlet of the concentrate pool is connected to the feed end of the vacuum concentrator through pipe D, and a pump D is installed on pipe D; the outlet of the clear liquid tank is connected to the cooking pot through pipe E, and a pump B is installed on pipe E.
4. The automated separation and preparation system for preparing fibers and extracts from mulberry branches according to claim 3, characterized in that: The vacuum concentrator is connected to a condensate tank, and the condensate tank is connected to the clear liquid tank via a pipe F, on which a pump C is installed.
5. The automated separation and preparation system for preparing fibers and extracts from mulberry branches according to claim 2, characterized in that: It also includes a filtrate tank, the filter press has a filtrate outlet for discharging filtrate, the filtrate outlet of the filter press is connected to the filtrate tank, the outlet of the filtrate tank is connected to a storage tank via a pipe G, and a pump E is installed on the pipe G.
6. The automated separation and preparation system for preparing fibers and extracts from mulberry branches according to claim 1, characterized in that: The discharge port of the cutting machine is connected to the inlet of the cooking pot via a belt conveyor; the cooking material outlet of the cooking pot is connected to the inlet of the peeling machine via a belt conveyor; the peel material outlet of the peeling machine is connected to the inlet of the surface black skin separator via a belt conveyor; and the bast skin outlet of the surface black skin separator is connected to the inlet of the microwave dryer via a belt conveyor.
7. The automated separation and preparation system for preparing fibers and extracts from mulberry branches according to claim 1, characterized in that: It also includes a dryer, wherein the skin outlet of the surface black skin separator is connected to the feed end of the dryer via a belt conveyor, and the dryer is used to dry the skin.
8. The automated separation and preparation system for preparing fibers and extracts from mulberry branches according to claim 2, characterized in that: The rod outlet of the peeling machine is connected to the feed inlet of the shredder via a belt conveyor; the discharge outlet of the shredder is connected to the feed inlet of the enzymatic hydrolysis chamber via a belt conveyor; and the discharge outlet of the enzymatic hydrolysis chamber is connected to the feed inlet of the grinder via a screw conveyor.
9. The automated separation and preparation system for preparing fibers and extracts from mulberry branches according to claim 1, characterized in that: A pump A is installed on pipe A between the outlet of the decoction pot and the inlet of the storage tank.
10. A streamlined separation and preparation system for preparing fibers and extracts using mulberry branches according to claim 2, characterized in that: A defoaming tank for removing fuzz from fine filamentous coarse materials is provided between the mill and the filter press.