WO2019052205A1 - Treatment method and equipment for waste residues in herbaceous fiber biological refining process - Google Patents

Treatment method and equipment for waste residues in herbaceous fiber biological refining process Download PDF

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Publication number
WO2019052205A1
WO2019052205A1 PCT/CN2018/086421 CN2018086421W WO2019052205A1 WO 2019052205 A1 WO2019052205 A1 WO 2019052205A1 CN 2018086421 W CN2018086421 W CN 2018086421W WO 2019052205 A1 WO2019052205 A1 WO 2019052205A1
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Prior art keywords
waste residue
fiber
steam
casing
debris
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PCT/CN2018/086421
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French (fr)
Chinese (zh)
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刘正初
苏维利
李云峰
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大庆天之草生物新材料科技有限公司
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Publication of WO2019052205A1 publication Critical patent/WO2019052205A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/80Destroying solid waste or transforming solid waste into something useful or harmless involving an extraction step
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/06Spray cleaning
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B5/00Operations not covered by a single other subclass or by a single other group in this subclass

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  • the present invention relates to the field of herbal fiber biorefinery. Specifically, it is a method and equipment for treating waste residue of herbal fiber bio-refining process.
  • the loss of more than 40% of the raw materials in the water body is causing serious “face pollution” to the environment and is facing a crisis that has been eliminated by history.
  • the chemical method of “cooking of caustic soda solution” is based on the fact that more than 35% of the raw materials (including a large amount of non-cellulosic and a little cellulose with low crystallinity) are hydrolyzed into monomer components, resulting in COD in high-concentration wastewater. With a value exceeding 10,000 mg/L, its application surface is being severely limited.
  • the transitional "bio-chemical combination” method invented in 1985 because there is no mechanism to get rid of the chemical hydrolysis, so that the COD value in the high concentration wastewater is maintained at about 10000 mg / L.
  • the modern biological method of "key enzyme directed cleavage of non-cellulose” invented in 1995 has not yet shown a strong driving force to promote the industrial technological revolution because it does not well break the constraints of "process and equipment support”.
  • the xylem the hemp-like agricultural products are called “hemp bones”
  • the epidermis the hemp-like agricultural products are called “hemp shells” attached to the fibrous agricultural products are mechanically compacted.
  • the cellulose turns into pieces and forms industrial waste.
  • the free water (about 35%) contained in the refined fiber is heated into steam to form industrial waste steam.
  • These industrial wastes and waste steam industry have become new problems in the manufacture of herbal fiber. There is no suitable method to solve it.
  • the technical problem solved by the invention is to overcome the shortcomings of the existing environment of the production of waste slag in the production process of the herbal fiber, and to provide a method for treating the waste residue of the herb fiber bio-refining process.
  • the herb fiber bio-refining process waste residue treatment method of the invention is used for treating the waste residue generated during the herbal fiber bio-refining process, and comprises the following steps:
  • the debris includes collecting debris through a dust collecting casing, and feeding the debris into the dust removing device to collect the debris by an extracting device that generates a negative pressure in the casing.
  • the mechanically stripping of the non-cellulosic organic matter produced by the inoculation device comprises: separating the solid matter in the waste liquid produced by the inoculating device by the solid-liquid separation device, that is, mechanically stripping the non-cellulosic organic matter fragments produced by the inoculating device.
  • the non-cellulosic organic matter in the storage device is sent to a milling device for grinding, and the finely ground powder is used as a matrix for the biomass material.
  • the mechanical stripping of the non-cellulosic organic matter produced by the recovery specification finishing device, the drying device and the opening device comprises: collecting the debris through the dust collecting shell, and disassembling the scraping device by generating a negative pressure inside the casing. Feed the dust collector to collect the debris together.
  • the method further comprises screening the ground powder to refine the coarse powder that has not been screened.
  • the method further comprises the step of treating the waste steam, wherein the waste steam refers to steam formed by heating and drying the refined fiber in the drying process of the herbal fiber bioremediation process, and must be discharged in time.
  • the waste steam refers to steam formed by heating and drying the refined fiber in the drying process of the herbal fiber bioremediation process, and must be discharged in time.
  • the steam extracted from the drying device is sent to the fermentation device, and direct atomization can increase the temperature and humidity in the fermentation device.
  • the steam extracted from the drying device is delivered to the inactivation device and/or the oil slick device to increase the temperature within the inactivation device and/or the oil slick device.
  • the steam extracted from the drying device is sent to an emulsified oil blending tank and/or a hot water storage tank for emulsification oil for the oil staining device.
  • the invention also provides a herb fiber bio-refining process waste residue treatment device, the device comprising:
  • the collecting device comprises a dust collecting shell covering the non-cellulosic organic matter pieces mechanically separated outside the standard finishing device, the drying device and the opening device, an extracting device applying a negative pressure to the dust collecting shell, and an inoculating device a solid-liquid separation device connected, the liquid-liquid separation device separating the liquid in the waste generated by the inoculating device from the debris;
  • a dust removing device comprising a dust removing housing connected to the extracting device to receive debris from the extracting device, the dust removing device capturing debris and collecting the debris together;
  • a storage device for receiving and storing debris collected in the dust removal device and debris transported by the solid-liquid separation device
  • a transport device having one end connected to the storage device
  • a milling device that receives debris from the transport device and grinds it
  • a sample sieve for screening the finely ground powder of the milling device to cause the fine powder to fall through the mesh eye while leaving the coarse powder on the sample sieve;
  • the intercepting device, the sample sieve and the grinding device are connected, and the coarse powder on the sample sieve is transported to the grinding device to be ground again;
  • a packing device that packs the ground powder.
  • the dust collecting housing includes a first housing that covers the outside of the specification finishing device, a second housing that covers the outside of the drying device, and a cover that covers the outside of the opening device.
  • the three housings have funnel shapes on the bottom walls of the first housing, the second housing and the third housing, and the funnel-shaped bottom portion is provided with a dust outlet.
  • the apparatus further comprises a conduit for extracting steam from the drying unit to the fermentation unit and/or the inactivation unit and/or the oil staining unit and/or the emulsified oil mixing tank and/or the hot water storage tank.
  • the pipe comprises a main pipe connecting the drying device and the hot water storage tank, a first branch pipe connecting the main pipe and the fermentation device, a second branch pipe connecting the main pipe and the inactivation device, and connecting.
  • a third branch pipe of the main pipe and the emulsified oil blending tank, a fourth branch pipe connecting the main pipe and the oil slick device, and the main pipe is provided with an air blowing device.
  • the herb fiber bio-refining process waste residue treating apparatus and method of the invention have the following beneficial effects:
  • the coarse powder that has not passed the screening is ground again, so that the coarse powder is not wasted.
  • the debris can be used more fully while ensuring that the size of the powder meets the set requirements.
  • the steam extracted from the drying device is sent to the emulsified oil mixing tank to heat the emulsified oil to make full use of the heat energy of the steam.
  • the steam in the drying device is introduced into the hot water storage tank, on the one hand, the water in the water can be heated.
  • the water generated by the steam condensation is distilled water, and does not contain any impurities, so that the hot water storage tank can be diluted. Impurities inside, thereby improving the quality of the water.
  • FIG. 1 is a schematic view showing the structure of a waste residue treatment portion of a waste fiber treatment equipment for a herb fiber biorefinery process according to an embodiment of the present invention.
  • FIG. 2 is a schematic structural view of an exhaust steam treatment part of a waste fiber treatment equipment for a herb fiber biorefinery process according to an embodiment of the present invention.
  • a standard finishing device b inoculation device, c drying device, d opening device, e fermentation device, f inactivation device, g emulsified oil mixing tank, h oil storage device, k hot water storage tank.
  • 1 dust collecting housing 1a first housing, 1b second housing, 1c third housing, 1d feeding port, 1e discharging port, 1f dust outlet, 2 extraction device, 3 solid-liquid separation device, 4 dust removal device, 41 dust removal housing, 42 water mist nozzle, 5 storage device, 6 transportation device, 7 milling device, 8 sample sieve, 9 intercept device, 10 packing device, 11 main pipe, 12 first pipe, 13 second sub-pipe, 14 third sub-pipe, 15 fourth sub-pipe, 16 blast device.
  • the herbal fiber in the present invention refers to various hemp plants such as hemp, ramie, kenaf, and fibers such as cotton fibers.
  • a large amount of mechanically stripped non-cellulosic organic matter is generated. If it is directly discharged into the atmosphere or water, it will cause waste of tissue-type non-cellulosic organic matter such as xylem and epidermis. It can cause serious pollution to air and water.
  • the invention provides a method for treating waste residue of a herb fiber bio-refining process, which can comprehensively treat the waste residue generated in the process of bio-refining of the herb fiber, so that it does not become an environmental pollutant and realizes the best use thereof, including the following steps:
  • the debris generated by the three devices of the specification finishing device, the drying device and the opening device is dry debris, which is easy to pollute the air, collects debris through the dust collecting shell, and generates an extraction device for generating a negative pressure in the casing. Send the debris to the dust collector to collect the debris together.
  • the debris generated by the inoculating device is mixed with the bacterial liquid to form a waste residue, and the solid matter in the waste liquid generated by the inoculating device needs to be separated by a solid-liquid separation device, wherein the solid matter is mechanically stripped non-cellulosic organic matter fragments produced by the inoculating device.
  • the herb fiber bio-refining process waste residue treatment method of the invention recovers the fragments, and the finely ground and finely ground powder is used as a matrix for preparing the biomass material, not only solves the pollution problem, but also mechanically peels off the non-cellulosic organic matter fragments. designation.
  • the method of the present invention further comprises screening the ground powder to ensure that the size of the substrate as the biomass material is in accordance with the set size.
  • the size of the fine powder selected by the screening is smaller than Or equal to 50 ⁇ m.
  • the coarse powder that has not passed through the screening may be ground again so that the coarse powder is not wasted. The ground powder is then packaged for transport and storage.
  • the steam generated when the wet fibers (water content is generally 40% or more) is dried with a large amount of heat, such as direct discharge into the air, which causes waste of energy.
  • the method of the invention further comprises the step of treating the waste steam, wherein the waste steam refers to steam formed by heating and drying the refined fiber in the drying process of the herb fiber, and the steam must be discharged in time, and the temperature is greater than or equal to 90. °C. Specifically, the following steps are included:
  • the steam extracted from the drying device is sent to the fermentation device, and the steam enters the fermentation device in a spray manner.
  • the fermentation unit requires heating to maintain a temperature that allows the fungus to multiply rapidly. Steam spray can increase the heat and humidity inside the fermentation unit.
  • the steam extracted from the drying device is delivered to the inactivation device and/or the oil slick device to increase the temperature within the inactivation device and/or the oil slick device.
  • the steam extracted from the drying device is sent to the emulsified oil mixing tank.
  • the steam is released under the surface of the emulsified oil or the oil collecting tank.
  • the pressure of the steam is passed through the emulsified oil having a height of 1000 mm or more, so that the heat of the steam can be fully utilized to heat the emulsified oil.
  • the pressure of the steam can be supplied by a blower.
  • the steam extracted from the drying device is sent to the hot water used to inactivate the hot water storage tank in which the device is inactivated.
  • steam is delivered to the hot water and the pressure of the steam is passed through a layer of water having a height greater than or equal to 1000 mm.
  • the invention also provides a herb fiber bio-refining process waste residue treatment device, by which the herb fiber bio-refining process waste residue treatment method of the invention can be implemented.
  • the equipment includes a waste residue management part.
  • the waste residue management part specifically includes: a collecting device, a dust removing device 4, a storage device 5, a transport device 6, a milling device 7, a sample sieve 8, a trap device 9, and a packing device. 10.
  • the collecting device comprises a dust collecting shell 1 for collecting mechanically stripping non-cellulosic organic matter fragments outside the standard finishing device a, the drying device c and the opening device d, and applying a negative pressure to the dust collecting housing 1
  • the lifting device 2 and the solid-liquid separating device 3 connected to the inoculating device b.
  • the extracting device 2 can be installed on a pipe connecting the dust collecting housing 1 and the storage device 5.
  • the extracting device 2 can be a blower installed at a position close to the dust collecting housing 1, or A rotary vane type fan installed at a position away from the dust collecting housing 1.
  • the solid-liquid separation device 3 is installed on a pipe connecting the inoculating device b and the storage device 5.
  • the solid-liquid separation pump can be used to separate the liquid in the waste generated by the inoculating device b from the mechanically stripped non-cellulosic organic matter. .
  • the debris is confined in the dust collecting casing 1 to prevent the debris from being scattered in the air to pollute the environment, and the dust collecting casing 1 may be covered in the specification finishing device a, the drying device c and the opening device d
  • An external outer casing may also be a plurality of independent casings respectively disposed outside the specification finishing device a, the drying device c, and the opening device d. The latter is used in this embodiment, specifically:
  • a first casing 1a is provided outside the specification finishing device a, a second casing 1b is provided outside the drying device c, and a third casing 1c is provided outside the opening device d.
  • the first casing 1a, the second casing 1b, and the third casing 1c each have a feed port 1d that allows the raw material of the herb fiber to be input into the casing, and a discharge port 1e that allows the raw material output casing of the herb fiber to be produced, and
  • the height of the feed port 1d is less than or equal to 50 mm, and the height of the discharge port 1e is less than or equal to 40 mm.
  • the bottom walls of the first casing, the second casing and the third casing are all funnel-shaped, and the funnel-shaped bottom is provided with a dust outlet 1f, and the debris can be under the action of gravity It is conveyed to the dust outlet 1f along the inclined surface of the funnel.
  • the dust removing device 4 includes a dust removing casing 41 connected to the extracting device 2 to receive debris from the extracting device 2, the dust removing device 4 capturing and collecting the debris together.
  • the dust removing device 4 is a water film dust removing device 4, and the dust removing housing 41 further includes a water mist head 42 that is sprayed into the dust removing housing 41 to form a water film that captures debris particles. Capture the debris through the water film and concentrate it on one piece.
  • the bottom wall of the dust removing housing 41 forms a slanted baffle so that the debris concentrated by the water film is moved by gravity into the storage device 5, and there is no need to additionally provide a device for extracting and transporting debris, which can make the mechanism of the entire device more Simple and compact.
  • the storage device 5 is for receiving and storing the debris collected in the dust removing device 4 and the solid or debris transported by the solid-liquid separating device 3.
  • the bottom wall of the housing of the storage device 5 forms an inclined baffle to move the debris to the transport device 6 by gravity.
  • the transport device 6 is connected to the storage device 5, and the other end is connected to the milling device 7, and the debris in the storage device 5 is transported to the milling device 7.
  • the transport device 6 has an inclined conveyor belt, the lower end of which is connected to the storage device 5, and the higher end extends to the upper end of the milling device 7, so that the transported debris falls on the grinding by gravity.
  • the feed port of the powder device 7 is inside.
  • the grinding device 7 grinds the chips, and the ground powder can be used as a substrate for preparing the biomass material, so that the chips can be fully utilized.
  • the sample sieve 8 screens the finely ground powder of the milling device 7 so that the fine powder falls through the mesh while leaving the coarse powder on the sample sieve 8.
  • the sieve opening of the sample sieve 8 is greater than or equal to 300 mesh, so that the size of the powder passing through the mesh of the sample sieve 8 is less than or equal to 50 ⁇ m.
  • the apparatus further includes a packing device 10 for packing the fine powder passing through the sample screen 8.
  • the sample screen 8 includes a sieve body and a high frequency vibration device (not shown) for driving the vibration of the screen body, and one end of the screen body is connected with the milling device 7 to receive the ground fine
  • the powder has a shrinkage discharge port at the other end, and the coarse powder remaining on the sieve body is output through the discharge port and sent to the milling device 7.
  • the apparatus further includes an intercepting device 9 that is connected to the sample sieve 8 and the milling device 7 to transport the coarse powder on the sample sieve 8 to the grinding device 7 to be reground.
  • the setting of the intercepting device 9 avoids the coarse powder. The waste can make more use of the debris while ensuring that the size of the powder meets the set requirements.
  • the apparatus of the present invention can also utilize the waste steam generated in the drying device c through the waste steam utilization portion, and the waste steam utilization portion includes extracting steam from the drying device to the fermentation device and/or the inactivation device and/or the oil stain.
  • the apparatus includes extracting steam from the drying device c and delivering the extracted steam to a delivery conduit within the fermentation device e.
  • the steam enters the housing of the fermentation unit e in the form of a spray, increasing the temperature and humidity within the housing.
  • the apparatus also includes a delivery conduit for delivering the extracted vapor to the inactivation device f and/or the oil rinsing device h to increase the temperature within the inactivation device f and/or the oil slick device h.
  • the conveying pipe that transports the steam to the oil slicker h communicates with the bottom of the oil sump h.
  • the apparatus also includes a delivery conduit for delivering the extracted vapor to the emulsified oil blending tank g that modulates the emulsified oil.
  • the conveying pipe which transports the steam to the emulsified oil mixing tank g extends into the liquid surface of the emulsified oil to release the steam and the released steam passes through the emulsified oil having a height of 1000 mm or more.
  • the device further comprises a conveying pipe for conveying the extracted steam to the hot water storage tank k, and the hot water storage tank k can heat the water therein, on the other hand, the water generated by the steam condensation is distilled water, Contains any impurities to dilute the impurities in the hot water storage tank k, thereby improving the quality of the water.
  • the conveying pipe that transports the steam to the hot water storage tank k extends below the liquid surface of the hot water to release the steam and the released steam passes through a water layer having a height greater than or equal to 1000 mm to perform sufficient heat exchange, thereby utilizing the steam more efficiently.
  • the heat is
  • the main pipe 11 is connected to the drying device c and the hot water storage tank k, and the air blowing device 16 is disposed on the main pipe 11, and the main pipe 11 is disposed near one end of the hot water storage tank k.
  • a pressure control valve (not shown). When the steam pressure in the main pipe 11 reaches the control pressure of the pressure control valve, the valve is opened, and when the steam pressure is less than the control pressure, the valve is closed.
  • the fermentation device e is connected to the main pipe 11 through the first branch pipe 12, the deactivating device f is connected to the main pipe 11 through the second branch pipe 13, and the emulsified oil mixing tank g is connected to the main pipe 11 through the third branch pipe 14, the oil is contaminated
  • the device h is connected to the main pipe 11 through a fourth branch pipe 15.
  • the ends of the first sub-duct 12, the second sub-duct 13, the third sub-duct 14 and the fourth sub-duct 15 are each provided with a sub-pipe valve (not shown), and the sub-pipe valve is normally closed and needs to be used. When steam is available, open the corresponding valve.

Abstract

A treatment equipment and method for waste residues in a herbaceous fiber biological refining process. The treatment equipment comprises a collecting device, a dust removal device (4), a storage device (5), a transport device (6), a milling device (7), a separation sieve (8), an interception device (9), and a packing device (10). The treatment method comprises the following steps: 1. recycling mechanically stripped non-cellulosic organic debris generated by a standardizing and finishing device (a), an inoculating device (b), a drying device (c), and an opening device (d); 2. gathering the mechanically stripped non-cellulosic organic debris and delivering same to the storage device (5); and 3. delivering the mechanically stripped non-cellulosic organic debris in the storage device (5) to the milling device (7) for milling, and using powder obtained by the milling as a basic substance of a biomass material.

Description

一种草本纤维生物精制工艺废渣治理方法及设备Herbal fiber bio-refining process waste residue treatment method and equipment 技术领域Technical field
本发明涉及草本纤维生物精制领域。具体为一种草本纤维生物精制工艺废渣治理方法及设备。The present invention relates to the field of herbal fiber biorefinery. Specifically, it is a method and equipment for treating waste residue of herbal fiber bio-refining process.
背景技术Background technique
从草本纤维原料中提取纤维用作纺织、造纸、生物质产业的基础材料,已有几千年历史。沿袭数千年之久的“沤麻”方法——将草本纤维植物茎秆砍到自然堆放在田间或运输并浸泡于江河湖沟等天然水体中,在天然菌群随机降解作用下剥离非纤维素的方法,存在不适宜工业化生产、纤维产量和品质不稳定、劳动强度大且环境恶劣(几乎没有人愿意从事“沤麻”这种农活了)等问题。尤其是与我国蓬勃发展的水产养殖业争夺水源的矛盾日益突出,占原料40%以上的脱落物流失在水体中,对环境造成严重的“面污染”,正面临着被历史所淘汰的危机。以“烧碱溶液蒸煮为中心”的化学方法,由于占原料35%以上的脱落物(包括大量非纤维素和少许结晶度不高的纤维素)被水解为单体成分,导致高浓度废水中COD值超过10000mg/L,其应用面正在受到严重限制。1985年发明的过渡型“生物-化学联合”方法,因为没有摆脱化学水解作用机制,以至于高浓度废水中COD值维持在10000mg/L左右。1995年发明的“关键酶定向裂解非纤维素”的现代生物方法,由于没有很好地破解“工艺与装备配套”的制约因子,至今尚未显现出推进产业技术革命的强劲动力。The extraction of fiber from herbal fiber raw materials has been used as a basic material for the textile, paper and biomass industries for thousands of years. The “ramie” method that has been inherited for thousands of years—cut the stalks of herbaceous fiber plants into natural piles in the field, transport them and soak them in natural water bodies such as rivers and lakes, and strip non-fibres under the random degradation of natural flora. There are problems such as unsuitable industrial production, unstable fiber production and quality, high labor intensity and harsh environment (almost no one is willing to engage in “rice” farming). In particular, the contradiction between China and the booming aquaculture industry is becoming more and more prominent. The loss of more than 40% of the raw materials in the water body is causing serious “face pollution” to the environment and is facing a crisis that has been eliminated by history. The chemical method of “cooking of caustic soda solution” is based on the fact that more than 35% of the raw materials (including a large amount of non-cellulosic and a little cellulose with low crystallinity) are hydrolyzed into monomer components, resulting in COD in high-concentration wastewater. With a value exceeding 10,000 mg/L, its application surface is being severely limited. The transitional "bio-chemical combination" method invented in 1985, because there is no mechanism to get rid of the chemical hydrolysis, so that the COD value in the high concentration wastewater is maintained at about 10000 mg / L. The modern biological method of "key enzyme directed cleavage of non-cellulose" invented in 1995 has not yet shown a strong driving force to promote the industrial technological revolution because it does not well break the constraints of "process and equipment support".
本申请人获得了“一种功能菌株用于工厂化发酵快速提取草本纤维的方法”等发明专利授权,并先后申请了“一种草本纤维原料规范整理设备及方法”、“一种生物精制草本纤维的自动化运转系统及方法”等一系列专利,这些技术方案从根本上解决了现代生物技术在草本纤维制造业中应用的关键技术。然而,草本纤维原料规范整理过程中,通过机械碾压作用,附着在纤维质农产品上的木质部(麻类农产品称“麻骨”)和表皮(麻类农产品称“麻壳”)等组织型非纤维素变成了碎片,形成了工业废渣。同时,精制纤维烘干工序中,通过加热使精制纤维所含游离水(35%左右)变成了蒸汽,形成了工业废汽。这些工业废渣、废汽业已成为草本纤维制造业的新问题,目前还没有合适的方法予以解决。The applicant obtained the invention patent authorization of “a method for rapidly extracting herbal fiber from a functional strain for industrial fermentation”, and applied for “a standard equipment and method for preparing herbal fiber raw materials” and “a bio-refined herb”. A series of patents such as the automated operation system and method of fiber, these technical solutions fundamentally solve the key technologies of modern biotechnology in the application of herbal fiber manufacturing. However, in the process of standardizing the preparation of herbal fiber raw materials, the xylem (the hemp-like agricultural products are called “hemp bones”) and the epidermis (the hemp-like agricultural products are called “hemp shells”) attached to the fibrous agricultural products are mechanically compacted. The cellulose turns into pieces and forms industrial waste. At the same time, in the drying process of the refined fiber, the free water (about 35%) contained in the refined fiber is heated into steam to form industrial waste steam. These industrial wastes and waste steam industry have become new problems in the manufacture of herbal fiber. There is no suitable method to solve it.
发明内容Summary of the invention
本发明解决的技术问题在于克服现有的草本纤维生产过程中产生废渣污染环境的缺点,提供一种草本纤维生物精制工艺废渣治理方法。The technical problem solved by the invention is to overcome the shortcomings of the existing environment of the production of waste slag in the production process of the herbal fiber, and to provide a method for treating the waste residue of the herb fiber bio-refining process.
本发明的草本纤维生物精制工艺废渣治理方法,用于治理草本纤维生物精制工艺过程中产生的废渣,包括以下步骤:The herb fiber bio-refining process waste residue treatment method of the invention is used for treating the waste residue generated during the herbal fiber bio-refining process, and comprises the following steps:
(1)回收规范整理装置、接种装置、烘干装置和开松装置产生的机械剥离非纤维素有机物碎片;其中,回收规范整理装置、烘干装置和开松装置产生的机械剥离非纤维素有机物碎片包括:通过收尘壳体收集碎片,通过使所述壳体内产生负压的提取装置将碎片送入除尘装置将碎片集中在一起。回收接种装置产生的机械剥离非纤维素有机物碎片包括:通过固液分离装置分离接种装置产生的废液中的固态物质,即接种装置产生的机械剥离非纤维素有机物碎片。(1) mechanically stripping non-cellulosic organic matter fragments produced by the standardizing finishing device, the inoculating device, the drying device and the opening device; wherein the mechanical separation of the non-cellulosic organic matter by the standard finishing device, the drying device and the opening device is recovered The debris includes collecting debris through a dust collecting casing, and feeding the debris into the dust removing device to collect the debris by an extracting device that generates a negative pressure in the casing. The mechanically stripping of the non-cellulosic organic matter produced by the inoculation device comprises: separating the solid matter in the waste liquid produced by the inoculating device by the solid-liquid separation device, that is, mechanically stripping the non-cellulosic organic matter fragments produced by the inoculating device.
(2)将机械剥离非纤维素有机物碎片集中送入储存装置;(2) concentrating the mechanically stripped non-cellulosic organic matter into a storage device;
(3)将储存装置内的非纤维素有机物碎片送入磨粉装置进行磨细,磨细的粉末用作生物质材料的基质。(3) The non-cellulosic organic matter in the storage device is sent to a milling device for grinding, and the finely ground powder is used as a matrix for the biomass material.
作为优选的方案,回收规范整理装置、烘干装置和开松装置产生的机械剥离非纤维素有机物碎片包括:通过收尘壳体收集碎片,通过使所述壳体内产生负压的提取装置将碎片送入除尘装置将碎片集中在一起。Preferably, the mechanical stripping of the non-cellulosic organic matter produced by the recovery specification finishing device, the drying device and the opening device comprises: collecting the debris through the dust collecting shell, and disassembling the scraping device by generating a negative pressure inside the casing. Feed the dust collector to collect the debris together.
作为优选的方案,所述方法还包括对磨细后的粉末进行筛选,将未通过筛选的粗粉再次磨细。Preferably, the method further comprises screening the ground powder to refine the coarse powder that has not been screened.
作为优选的方案,还包括对废汽进行治理的步骤,所述废汽是指草本纤维生物精制工艺过程中烘干装置加热烘干精制纤维所形成而又必须及时排出的蒸汽。As a preferred solution, the method further comprises the step of treating the waste steam, wherein the waste steam refers to steam formed by heating and drying the refined fiber in the drying process of the herbal fiber bioremediation process, and must be discharged in time.
作为优选的方案,将从烘干装置抽取的蒸汽输送至发酵装置,直接雾化可提高发酵装置内的温度和湿度。As a preferred solution, the steam extracted from the drying device is sent to the fermentation device, and direct atomization can increase the temperature and humidity in the fermentation device.
作为优选的方案,将从烘干装置抽取的蒸汽输送至灭活装置和/或渍油装置内提高灭活装置和/或渍油装置内的温度。As a preferred solution, the steam extracted from the drying device is delivered to the inactivation device and/or the oil slick device to increase the temperature within the inactivation device and/or the oil slick device.
作为优选的方案,将从烘干装置抽取的蒸汽输送至为渍油装置调制乳化油的乳化油调配槽和/或热水储存槽内。As a preferred solution, the steam extracted from the drying device is sent to an emulsified oil blending tank and/or a hot water storage tank for emulsification oil for the oil staining device.
本发明还提供一种草本纤维生物精制工艺废渣治理设备,所述设备包括:The invention also provides a herb fiber bio-refining process waste residue treatment device, the device comprising:
收集装置,包括罩在规范整理装置、烘干装置和开松装置外部收集机械剥离非纤维素有机物碎片的收尘壳体、对所述收尘壳体施加负压的抽提装置和与接种装置连接的固液分离装置,所述固液分离装置将接种装置产生的废渣中的液体与碎片分离开;The collecting device comprises a dust collecting shell covering the non-cellulosic organic matter pieces mechanically separated outside the standard finishing device, the drying device and the opening device, an extracting device applying a negative pressure to the dust collecting shell, and an inoculating device a solid-liquid separation device connected, the liquid-liquid separation device separating the liquid in the waste generated by the inoculating device from the debris;
除尘装置,包括与所述抽提装置连接以接收来自所述抽提装置的碎片的除尘壳体,所述除尘装置捕获碎片并将碎片集中在一起;a dust removing device comprising a dust removing housing connected to the extracting device to receive debris from the extracting device, the dust removing device capturing debris and collecting the debris together;
储存装置,用来接收并储存除尘装置集中的碎片及固液分离装置输送来的碎片;a storage device for receiving and storing debris collected in the dust removal device and debris transported by the solid-liquid separation device;
运输装置,一端与所述储存装置连接;a transport device having one end connected to the storage device;
磨粉装置,所述磨粉装置接收所述运输装置运来的碎片并对其进行磨细;a milling device that receives debris from the transport device and grinds it;
分样筛,所述分样筛对所述磨粉装置磨细的粉末进行筛选使细粉通过筛眼落下同时使粗粉留在分样筛上;a sample sieve for screening the finely ground powder of the milling device to cause the fine powder to fall through the mesh eye while leaving the coarse powder on the sample sieve;
截留装置,分样筛和磨粉装置连接将分样筛上的粗粉输送至磨粉装置再次磨细;The intercepting device, the sample sieve and the grinding device are connected, and the coarse powder on the sample sieve is transported to the grinding device to be ground again;
打包装置,对磨细的粉末进行打包。A packing device that packs the ground powder.
作为优选的方案,所述收尘壳体包括罩在所述规范整理装置外部的第一壳体、罩在所述烘干装置外部的第二壳体和罩在所述开松装置外部的第三壳体,所述第一壳体、第二壳体和第三壳体的底壁呈漏斗状,所述漏斗状的底部设有出尘口。Preferably, the dust collecting housing includes a first housing that covers the outside of the specification finishing device, a second housing that covers the outside of the drying device, and a cover that covers the outside of the opening device. The three housings have funnel shapes on the bottom walls of the first housing, the second housing and the third housing, and the funnel-shaped bottom portion is provided with a dust outlet.
作为优选的方案,所述设备还包括从烘干装置抽取蒸汽输送至发酵装置和/或灭活装置和/或渍油装置和/或乳化油调配槽和/或热水储存槽的管道。Preferably, the apparatus further comprises a conduit for extracting steam from the drying unit to the fermentation unit and/or the inactivation unit and/or the oil staining unit and/or the emulsified oil mixing tank and/or the hot water storage tank.
作为优选的方案,所述所述管道包括连接烘干装置与热水储存槽的主管道、连接主管道与发酵装置的第一分管道、连接主管道与灭活装置的第二分管道、连接主管道与乳化油调配槽的第三分管道、连接主管道与渍油装置的第四分管道,所述主管道上设置有鼓风装置。Preferably, the pipe comprises a main pipe connecting the drying device and the hot water storage tank, a first branch pipe connecting the main pipe and the fermentation device, a second branch pipe connecting the main pipe and the inactivation device, and connecting. a third branch pipe of the main pipe and the emulsified oil blending tank, a fourth branch pipe connecting the main pipe and the oil slick device, and the main pipe is provided with an air blowing device.
本发明的草本纤维生物精制工艺废渣治理设备和方法与现有技术相比,具有以下有益效果:Compared with the prior art, the herb fiber bio-refining process waste residue treating apparatus and method of the invention have the following beneficial effects:
1、将碎片收集、集中并磨细,一方面可防止碎片污染大气环境,同时利用磨细的粉末作为制备生物质材料的基质,充分利用了碎片中的有机质,起到了变废为宝的效果。1. Collect, concentrate and grind the debris. On the one hand, it can prevent the debris from polluting the atmospheric environment. At the same time, the fine powder is used as the matrix for preparing the biomass material, and the organic matter in the debris is fully utilized, which has turned the waste into treasure. .
2、将未通过筛选的粗粉再次磨细,这样不会使粗粉被浪费掉。可更充分地利用碎片,同时保证粉末的尺寸符合设定的要求。2. The coarse powder that has not passed the screening is ground again, so that the coarse powder is not wasted. The debris can be used more fully while ensuring that the size of the powder meets the set requirements.
3、将烘干装置内的蒸汽引入发酵装置,提高其内的温度和湿度,从而节约了能源。3. Introduce the steam in the drying device into the fermentation device to increase the temperature and humidity inside, thereby saving energy.
4、将烘干装置内的蒸汽引入灭活装置和/或渍油装置,提高其内的温度。4. Introduce the steam in the drying device into the inactivation device and/or the oil slick device to increase the temperature inside.
5、将从烘干装置抽取的蒸汽输送至乳化油调配槽对乳化油进行加热,充分利用蒸汽的热能。5. The steam extracted from the drying device is sent to the emulsified oil mixing tank to heat the emulsified oil to make full use of the heat energy of the steam.
6、将烘干装置内的蒸汽引入热水储存槽,一方面可对其内的水进行加热,另一方面,蒸汽冷凝生成的水为蒸馏水,不含任何杂质,从而可稀释热水储存槽内的杂质,从而提高水的质量。6. The steam in the drying device is introduced into the hot water storage tank, on the one hand, the water in the water can be heated. On the other hand, the water generated by the steam condensation is distilled water, and does not contain any impurities, so that the hot water storage tank can be diluted. Impurities inside, thereby improving the quality of the water.
附图说明DRAWINGS
图1为本发明一个实施例的草本纤维生物精制工艺废渣治理设备的废渣治理部分的结构示意图。BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic view showing the structure of a waste residue treatment portion of a waste fiber treatment equipment for a herb fiber biorefinery process according to an embodiment of the present invention.
图2为本发明一个实施例的草本纤维生物精制工艺废渣治理设备的废汽治理部分的结构示意图。2 is a schematic structural view of an exhaust steam treatment part of a waste fiber treatment equipment for a herb fiber biorefinery process according to an embodiment of the present invention.
附图标记Reference numeral
a规范整理装置,b接种装置,c烘干装置,d开松装置,e发酵装置,f灭活装置,g乳化油调配槽,h渍油装置,k热水储存槽。a standard finishing device, b inoculation device, c drying device, d opening device, e fermentation device, f inactivation device, g emulsified oil mixing tank, h oil storage device, k hot water storage tank.
1收尘壳体,1a第一壳体,1b第二壳体,1c第三壳体,1d进料口,1e出料口,1f出尘口,2抽提装置,3固液分离装置,4除尘装置,41除尘壳体,42水雾喷头,5储存装置,6运输装置,7磨粉装置,8分样筛,9截留装置,10打包装置,11主管道,12第一分管道,13第二分管道,14第三分管道,15第四分管道,16鼓风装置。1 dust collecting housing, 1a first housing, 1b second housing, 1c third housing, 1d feeding port, 1e discharging port, 1f dust outlet, 2 extraction device, 3 solid-liquid separation device, 4 dust removal device, 41 dust removal housing, 42 water mist nozzle, 5 storage device, 6 transportation device, 7 milling device, 8 sample sieve, 9 intercept device, 10 packing device, 11 main pipe, 12 first pipe, 13 second sub-pipe, 14 third sub-pipe, 15 fourth sub-pipe, 16 blast device.
具体实施方式Detailed ways
本发明中的草本纤维指大麻、苎麻、红麻等各种麻类植物及棉纤维等纤维。在精草本纤维生物精制的过程中,会产生大量的机械剥离非纤维素有机物碎片,如果直接排放在大气或者水域中会导致其中的木质部和表皮等组织型非纤维素有机物质浪费掉,同时还会对空气和水域造成严重的污染。The herbal fiber in the present invention refers to various hemp plants such as hemp, ramie, kenaf, and fibers such as cotton fibers. In the process of bio-refining of refined herbal fiber, a large amount of mechanically stripped non-cellulosic organic matter is generated. If it is directly discharged into the atmosphere or water, it will cause waste of tissue-type non-cellulosic organic matter such as xylem and epidermis. It can cause serious pollution to air and water.
本发明提供了一种草本纤维生物精制工艺废渣治理方法,能综合治理草本纤维生物精制工艺过程中产生的废渣,使之不成为环境污染物且实现物尽其用,包括以下步骤:The invention provides a method for treating waste residue of a herb fiber bio-refining process, which can comprehensively treat the waste residue generated in the process of bio-refining of the herb fiber, so that it does not become an environmental pollutant and realizes the best use thereof, including the following steps:
(1)回收提取规范整理装置、接种装置、烘干装置和开松装置产生的机械剥离非纤维素有机物碎片。其中,这规范整理装置、烘干装置和开松装置这三种装置产生的碎片为干碎片,容易污染空气,可通过收尘壳体收集碎片,通过使所述壳体内产生负压的提取装置将碎片送入除尘装置将碎片集中在一起。接种装置产生的碎片与菌液混合在一起形成废渣,需要通过固液分离装置分离接种装置产生的废液中的固态物质,其中的固态物质是接种装置产生的机械剥离非纤维素有机物碎片。(1) Mechanical extraction of non-cellulosic organic matter fragments produced by the extraction and extraction finishing device, the inoculating device, the drying device, and the opening device. Wherein, the debris generated by the three devices of the specification finishing device, the drying device and the opening device is dry debris, which is easy to pollute the air, collects debris through the dust collecting shell, and generates an extraction device for generating a negative pressure in the casing. Send the debris to the dust collector to collect the debris together. The debris generated by the inoculating device is mixed with the bacterial liquid to form a waste residue, and the solid matter in the waste liquid generated by the inoculating device needs to be separated by a solid-liquid separation device, wherein the solid matter is mechanically stripped non-cellulosic organic matter fragments produced by the inoculating device.
(2)将机械剥离非纤维素有机物碎片集中送入储存装置,等待下一步处理。储存装置内的碎片的含水量不高于18%。(2) The mechanically stripped non-cellulosic organic matter fragments are collectively sent to the storage device, waiting for the next treatment. The moisture content of the debris in the storage device is not higher than 18%.
(3)将储存装置内的机械剥离非纤维素有机物碎片送入磨粉装置进行磨细,磨细的粉末作为制备生物质材料的基质。(3) The mechanically stripped non-cellulosic organic matter in the storage device is sent to a grinding device for grinding, and the finely ground powder is used as a substrate for preparing the biomass material.
以上对碎片的收集、提取、固液分离及碎片的储存、磨细、筛选和打包等操作可通过一切可行的方式来进行,优选的实现方式将在下面对相关的设备进行描述时予以介绍。The above operations for collecting, extracting, solid-liquid separation, and storing, grinding, screening, and packaging of debris can be performed in all feasible ways. The preferred implementation will be described below when describing related equipment.
本发明的草本纤维生物精制工艺废渣治理方法通过回收碎片,将碎片磨细,磨细的粉末作为制备生物质材料的基质,不仅可解决污染的问题,还对机械剥离非纤维素有机物碎片进行了充分的利用。The herb fiber bio-refining process waste residue treatment method of the invention recovers the fragments, and the finely ground and finely ground powder is used as a matrix for preparing the biomass material, not only solves the pollution problem, but also mechanically peels off the non-cellulosic organic matter fragments. designation.
作为优选,本发明的方法还包括对磨细后的粉末进行筛选,这样可保证作为制备生物质材料的基质的尺寸符合设定的尺寸,在本实施例中,通过筛选的细粉的尺寸小于或者等于50μm。作为进一步的优选,可将未通过筛选的粗粉再次磨细,这样不会使粗粉被浪费掉。然后对磨细的粉末进行打包使其便于运输和储藏。Preferably, the method of the present invention further comprises screening the ground powder to ensure that the size of the substrate as the biomass material is in accordance with the set size. In the present embodiment, the size of the fine powder selected by the screening is smaller than Or equal to 50μm. As a further preference, the coarse powder that has not passed through the screening may be ground again so that the coarse powder is not wasted. The ground powder is then packaged for transport and storage.
在纤维的制作过程中,对湿润的纤维(含水率一般高达40%及以上)进行烘干时产生的蒸汽带有大量的热量,如直接排放至空气中会造成能量的浪费。发明的方法进一步包括对废汽进行治理的步骤,所述废汽是指草本纤维生物精制工艺过程中烘干装置加热烘干精制纤维所形成而又必须及时排出的蒸汽,其温度大于或者等于90℃。具体包括以下步骤:In the production process of fibers, the steam generated when the wet fibers (water content is generally 40% or more) is dried with a large amount of heat, such as direct discharge into the air, which causes waste of energy. The method of the invention further comprises the step of treating the waste steam, wherein the waste steam refers to steam formed by heating and drying the refined fiber in the drying process of the herb fiber, and the steam must be discharged in time, and the temperature is greater than or equal to 90. °C. Specifically, the following steps are included:
将从烘干装置抽取的蒸汽输送至发酵装置,所述蒸汽以喷雾的方式进入发酵装置。发酵装置需要加热以保持使菌类大量快速繁殖的温度。蒸汽喷雾可以提高发酵装置内的热量和湿度。The steam extracted from the drying device is sent to the fermentation device, and the steam enters the fermentation device in a spray manner. The fermentation unit requires heating to maintain a temperature that allows the fungus to multiply rapidly. Steam spray can increase the heat and humidity inside the fermentation unit.
将从烘干装置抽取的蒸汽输送至灭活装置和/或渍油装置内提高灭活装置和/或渍油装置内的温度。The steam extracted from the drying device is delivered to the inactivation device and/or the oil slick device to increase the temperature within the inactivation device and/or the oil slick device.
将从烘干装置抽取的蒸汽输送至乳化油调配槽内。蒸汽是在乳化油或者集油槽的液面下释放,在本实施例中,蒸汽的压力使其穿过高度大于或等于1000mm的乳化油,这样可充分利用蒸汽的热量加热乳化油。蒸汽的压力可通过鼓风机来提供。The steam extracted from the drying device is sent to the emulsified oil mixing tank. The steam is released under the surface of the emulsified oil or the oil collecting tank. In the present embodiment, the pressure of the steam is passed through the emulsified oil having a height of 1000 mm or more, so that the heat of the steam can be fully utilized to heat the emulsified oil. The pressure of the steam can be supplied by a blower.
将从烘干装置抽取的蒸汽输送至用于灭活装置进行灭活的热水储存槽的热水中。在本实施例中,蒸汽输送至热水中且蒸汽的压力使其穿过高度大于或等于1000mm的水层。The steam extracted from the drying device is sent to the hot water used to inactivate the hot water storage tank in which the device is inactivated. In this embodiment, steam is delivered to the hot water and the pressure of the steam is passed through a layer of water having a height greater than or equal to 1000 mm.
本发明还提供一种草本纤维生物精制工艺废渣治理设备,利用该设备可以实施本发明的草本纤维生物精制工艺废渣治理方法。该设备包括废渣治理部分,如图1所示,废渣治理部分具体包括:收集装置、除尘装置4、储存装置5、运输装置6、磨粉装置7、分样筛8、截留装置9和打包装置10。The invention also provides a herb fiber bio-refining process waste residue treatment device, by which the herb fiber bio-refining process waste residue treatment method of the invention can be implemented. The equipment includes a waste residue management part. As shown in FIG. 1 , the waste residue management part specifically includes: a collecting device, a dust removing device 4, a storage device 5, a transport device 6, a milling device 7, a sample sieve 8, a trap device 9, and a packing device. 10.
其中,收集装置包括罩在规范整理装置a、烘干装置c和开松装置d外部收集机械剥离非纤维素有机物碎片的收尘壳体1、对所述收尘壳体1施加负压的抽提装置2和与接种装置b连接的固液分离装置3。在本实施例中,抽提装置2可安装在连接收尘壳体1和储存装置5之间的管道上,抽提装置2可采用安装在靠近收尘壳体1的位置的鼓风机,或者采用安装在远离收尘壳体1的位置的旋片式抽风机。所述固液分离装置3安装在连接接种装置b与储存装置5之间的管道上,可采用固液分离泵,将接种装置b产生的废渣中的液体与机械剥离非纤维素有机物碎片分离开。Wherein, the collecting device comprises a dust collecting shell 1 for collecting mechanically stripping non-cellulosic organic matter fragments outside the standard finishing device a, the drying device c and the opening device d, and applying a negative pressure to the dust collecting housing 1 The lifting device 2 and the solid-liquid separating device 3 connected to the inoculating device b. In the present embodiment, the extracting device 2 can be installed on a pipe connecting the dust collecting housing 1 and the storage device 5. The extracting device 2 can be a blower installed at a position close to the dust collecting housing 1, or A rotary vane type fan installed at a position away from the dust collecting housing 1. The solid-liquid separation device 3 is installed on a pipe connecting the inoculating device b and the storage device 5. The solid-liquid separation pump can be used to separate the liquid in the waste generated by the inoculating device b from the mechanically stripped non-cellulosic organic matter. .
在纤维的生产过程中,碎片被限制在收尘壳体1内,防止碎片飘散在空气中污染环境,收尘壳体1可以是罩在规范整理装置a、烘干装置c和开松装置d外部的一整个壳体,也可以是分别设置在规范整理装置a、烘干装置c和开松装置d外部的多个独立壳体。本实施例中采用后者,具体为:In the production process of the fiber, the debris is confined in the dust collecting casing 1 to prevent the debris from being scattered in the air to pollute the environment, and the dust collecting casing 1 may be covered in the specification finishing device a, the drying device c and the opening device d An external outer casing may also be a plurality of independent casings respectively disposed outside the specification finishing device a, the drying device c, and the opening device d. The latter is used in this embodiment, specifically:
在所述规范整理装置a外部设置第一壳体1a,在烘干装置c外部设置第二壳体1b,在开松装置d外部设置第三壳体1c。第一壳体1a、第二壳体1b和第三壳体1c均具有允许制作草本纤维的原料输入壳体内的进料口1d和允许制作草本纤维的原料输出壳体外的出料口1e,且所述进料口1d高度小于或等于50mm,出料口1e的高度小于或等于40mm。在本实施例中,所述第一壳体、第二壳体和第三壳体的底壁均呈漏斗状,所述漏斗状的底部设有出尘口1f,碎片可在重力的作用下沿漏斗的倾斜面输送至出尘口1f。A first casing 1a is provided outside the specification finishing device a, a second casing 1b is provided outside the drying device c, and a third casing 1c is provided outside the opening device d. The first casing 1a, the second casing 1b, and the third casing 1c each have a feed port 1d that allows the raw material of the herb fiber to be input into the casing, and a discharge port 1e that allows the raw material output casing of the herb fiber to be produced, and The height of the feed port 1d is less than or equal to 50 mm, and the height of the discharge port 1e is less than or equal to 40 mm. In this embodiment, the bottom walls of the first casing, the second casing and the third casing are all funnel-shaped, and the funnel-shaped bottom is provided with a dust outlet 1f, and the debris can be under the action of gravity It is conveyed to the dust outlet 1f along the inclined surface of the funnel.
除尘装置4包括与所述抽提装置2连接以接收来自所述抽提装置2的碎片的除尘壳体41,所述除尘装置4捕获并将碎片集中在一起。在本实施例中,所述除尘装置4为水膜除尘装置4,除尘壳体41还包括向所述除尘壳体41内喷雾以形成扑捉碎片颗粒的水膜的水雾喷头42。通过水膜捕捉碎片,使其集中在一块。所述除尘壳体41的底壁形成倾斜导流板使被水膜集中的碎片依靠重力移动至所述储存装置5内,不需要另外设置提取和运输碎片的装置,可使得整个设备的机构更简单和紧凑。The dust removing device 4 includes a dust removing casing 41 connected to the extracting device 2 to receive debris from the extracting device 2, the dust removing device 4 capturing and collecting the debris together. In the present embodiment, the dust removing device 4 is a water film dust removing device 4, and the dust removing housing 41 further includes a water mist head 42 that is sprayed into the dust removing housing 41 to form a water film that captures debris particles. Capture the debris through the water film and concentrate it on one piece. The bottom wall of the dust removing housing 41 forms a slanted baffle so that the debris concentrated by the water film is moved by gravity into the storage device 5, and there is no need to additionally provide a device for extracting and transporting debris, which can make the mechanism of the entire device more Simple and compact.
储存装置5用来接收并储存除尘装置4集中的碎片及固液分离装置3输送来的固体即碎片。在本实施例中,所述储存装置5的壳体的底壁形成倾斜导流板使碎片依靠重力移动至所述运输装置6上。The storage device 5 is for receiving and storing the debris collected in the dust removing device 4 and the solid or debris transported by the solid-liquid separating device 3. In the present embodiment, the bottom wall of the housing of the storage device 5 forms an inclined baffle to move the debris to the transport device 6 by gravity.
运输装置6的一端与所述储存装置5连接,另一端与磨粉装置7连接,将储存装置5内的碎片运输至磨粉装置7。在本实施例中,运输装置6具有倾斜的输送带,输送带较低的一端与储存装置5连接,较高的一端伸至磨粉装置7的上端,使被输送的碎片依靠重力落在磨粉装置7的入料口内。One end of the transport device 6 is connected to the storage device 5, and the other end is connected to the milling device 7, and the debris in the storage device 5 is transported to the milling device 7. In the present embodiment, the transport device 6 has an inclined conveyor belt, the lower end of which is connected to the storage device 5, and the higher end extends to the upper end of the milling device 7, so that the transported debris falls on the grinding by gravity. The feed port of the powder device 7 is inside.
所述磨粉装置7对碎片进行磨细,磨细后的粉末可作为制备生物质材料的基质,从而对碎片进行了充分的利用。The grinding device 7 grinds the chips, and the ground powder can be used as a substrate for preparing the biomass material, so that the chips can be fully utilized.
所述分样筛8对所述磨粉装置7磨细的粉末进行筛选使细粉通过筛眼落下同时使粗粉留在分样筛8上。在本实施例中,所述分样筛8的筛孔大于或等于300目,使得通过分样筛8的筛孔的粉末的尺寸小于或者等于50μm。设备还包括打包装置10,对通过分样筛8的细粉进行打包。The sample sieve 8 screens the finely ground powder of the milling device 7 so that the fine powder falls through the mesh while leaving the coarse powder on the sample sieve 8. In the present embodiment, the sieve opening of the sample sieve 8 is greater than or equal to 300 mesh, so that the size of the powder passing through the mesh of the sample sieve 8 is less than or equal to 50 μm. The apparatus further includes a packing device 10 for packing the fine powder passing through the sample screen 8.
在本实施例中,所述分样筛8包括筛体和驱动所述筛体震动的高频震动装置(图中未示出),所述筛体一端与磨粉装置7连接接收磨细的粉末,另一端形成收缩出料口,使留在所述筛体上的粗粉经由所述出料口输出并输送至磨粉装置7。In this embodiment, the sample screen 8 includes a sieve body and a high frequency vibration device (not shown) for driving the vibration of the screen body, and one end of the screen body is connected with the milling device 7 to receive the ground fine The powder has a shrinkage discharge port at the other end, and the coarse powder remaining on the sieve body is output through the discharge port and sent to the milling device 7.
所述设备还包括与所述分样筛8和磨粉装置7连接将分样筛8上的粗粉输送至磨粉装置7再次磨细的截留装置9,截留装置9的设置避免了粗粉的浪费,可更充分地利用碎片同时保证粉末的尺寸符合设定的要求。The apparatus further includes an intercepting device 9 that is connected to the sample sieve 8 and the milling device 7 to transport the coarse powder on the sample sieve 8 to the grinding device 7 to be reground. The setting of the intercepting device 9 avoids the coarse powder. The waste can make more use of the debris while ensuring that the size of the powder meets the set requirements.
本发明的设备还可以通过废蒸汽利用部分对烘干装置c内产生的废蒸汽进行利用,废蒸汽利用部分包括从烘干装置抽取蒸汽输送至发酵装置和/或灭活装置和/或渍油装置和/或乳化油调配槽和/或热水储存槽的管道。如图2所示,在本实施例中,具体通过以下结构来实现:The apparatus of the present invention can also utilize the waste steam generated in the drying device c through the waste steam utilization portion, and the waste steam utilization portion includes extracting steam from the drying device to the fermentation device and/or the inactivation device and/or the oil stain. A conduit for the device and/or emulsified oil blending tank and/or hot water storage tank. As shown in FIG. 2, in this embodiment, the following structure is specifically implemented:
所述设备包括从烘干装置c抽取蒸汽,将抽取的蒸汽输送至发酵装置e内的输送管道。所述蒸汽以喷雾的形式进入所述发酵装置e的壳体内,提高壳体内的温度和湿度。The apparatus includes extracting steam from the drying device c and delivering the extracted steam to a delivery conduit within the fermentation device e. The steam enters the housing of the fermentation unit e in the form of a spray, increasing the temperature and humidity within the housing.
所述设备还包括将抽取的蒸汽输送至灭活装置f和/或渍油装置h内提高灭活装置f和/或渍油装置h内的温度的输送管道。将蒸汽输送至渍油装置h内的输送管道与渍油装置h的底部相通。The apparatus also includes a delivery conduit for delivering the extracted vapor to the inactivation device f and/or the oil rinsing device h to increase the temperature within the inactivation device f and/or the oil slick device h. The conveying pipe that transports the steam to the oil slicker h communicates with the bottom of the oil sump h.
所述设备还包括将抽取的蒸汽输送至调制乳化油的乳化油调配槽g内的输送管道。将蒸汽输送至乳化油调配槽g内的输送管道伸入乳化油的液面下释放蒸汽且释放的蒸汽穿过高度大于或等于1000mm的乳化油。The apparatus also includes a delivery conduit for delivering the extracted vapor to the emulsified oil blending tank g that modulates the emulsified oil. The conveying pipe which transports the steam to the emulsified oil mixing tank g extends into the liquid surface of the emulsified oil to release the steam and the released steam passes through the emulsified oil having a height of 1000 mm or more.
所述设备还包括将抽取的蒸汽输送至热水储存槽k的输送管道,热水储存槽k,一方面可对其内的水进行加热,另一方面,蒸汽冷凝生成的水为蒸馏水,不含任何杂质,从而可稀释热水储存槽k内的杂质,从而提高水的质量。The device further comprises a conveying pipe for conveying the extracted steam to the hot water storage tank k, and the hot water storage tank k can heat the water therein, on the other hand, the water generated by the steam condensation is distilled water, Contains any impurities to dilute the impurities in the hot water storage tank k, thereby improving the quality of the water.
将蒸汽输送至热水储存槽k的输送管道伸入热水的液面下释放蒸汽且释放的蒸汽穿过高度大于或等于1000mm的水层,进行充分的热交换,从而更大效率地利用蒸汽的热量。The conveying pipe that transports the steam to the hot water storage tank k extends below the liquid surface of the hot water to release the steam and the released steam passes through a water layer having a height greater than or equal to 1000 mm to perform sufficient heat exchange, thereby utilizing the steam more efficiently. The heat.
在本实施例中,如图2所示,主管道11连接烘干装置c与热水储存槽k,鼓风装置16设置在主管道11上,主管道11靠近热水储存槽k的一端设有压力控制阀(图中未示出),当主管道11内蒸汽压力达到压力控制阀的控制压力时,阀门开启,当蒸汽压力小于控制压力时,阀门关闭。In the present embodiment, as shown in FIG. 2, the main pipe 11 is connected to the drying device c and the hot water storage tank k, and the air blowing device 16 is disposed on the main pipe 11, and the main pipe 11 is disposed near one end of the hot water storage tank k. There is a pressure control valve (not shown). When the steam pressure in the main pipe 11 reaches the control pressure of the pressure control valve, the valve is opened, and when the steam pressure is less than the control pressure, the valve is closed.
发酵装置e通过第一分管道12与主管道11连接,灭活装置f通过第二分管道13与主管道11连接,乳化油调配槽g通过第三分管道14与主管道11连接,渍油装置h通过第四分管道15与主管道11连接。第一分管道12、第二分管道13、第三分管道14和第四分管道15的末端均设有分管道阀门(图中未示出),分管道阀门是常闭的,在需要使用蒸汽时,打开相应的阀门即可。The fermentation device e is connected to the main pipe 11 through the first branch pipe 12, the deactivating device f is connected to the main pipe 11 through the second branch pipe 13, and the emulsified oil mixing tank g is connected to the main pipe 11 through the third branch pipe 14, the oil is contaminated The device h is connected to the main pipe 11 through a fourth branch pipe 15. The ends of the first sub-duct 12, the second sub-duct 13, the third sub-duct 14 and the fourth sub-duct 15 are each provided with a sub-pipe valve (not shown), and the sub-pipe valve is normally closed and needs to be used. When steam is available, open the corresponding valve.
以上实施例仅为本发明的示例性实施例,不用于限制本发明,本发明的保护范围由权利要求书限定。本领域技术人员在本发明的实质和保护范围内,对本发明做出的各种修改或等同替换也落在本发明的保护范围内。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 (26)

  1. 一种草本纤维生物精制工艺废渣治理方法,其特征在于,用于治理草本纤维生物精制工艺过程中产生的废渣,包括以下步骤:The invention relates to a method for treating waste residue of a herbal fiber biorefinery process, which is characterized in that the waste residue generated during the process of treating the herbal fiber biorefinement process comprises the following steps:
    (1)回收规范整理装置、接种装置、烘干装置和开松装置产生的机械剥离非纤维素有机物碎片;(1) mechanically stripping non-cellulosic organic matter fragments produced by the standard finishing device, the inoculating device, the drying device and the opening device;
    (2)将机械剥离非纤维素有机物碎片集中送入储存装置;(2) concentrating the mechanically stripped non-cellulosic organic matter into a storage device;
    (3)将储存装置内的机械剥离非纤维素有机物碎片送入磨粉装置进行磨细,磨细的粉末用作生物质材料的基质。(3) The mechanically stripped non-cellulosic organic matter in the storage device is sent to a milling device for grinding, and the finely ground powder is used as a matrix for the biomass material.
  2. 根据权利要求1所述的草本纤维生物精制工艺废渣治理方法,其特征在于,回收规范整理装置、烘干装置和开松装置产生的机械剥离非纤维素有机物碎片包括:通过收尘壳体收集碎片,通过使所述壳体内产生负压的提取装置将碎片送入除尘装置将碎片集中在一起。The method for treating a residue of a herb fiber biorefinery process according to claim 1, wherein the mechanically stripping the non-cellulosic organic matter generated by the reclaiming finishing device, the drying device and the opening device comprises: collecting the debris through the dust collecting shell. The debris is sent to the dust removing device to collect the debris by causing an extraction device that generates a negative pressure in the casing.
  3. 根据权利要求1所述的草本纤维生物精制工艺废渣治理方法,其特征在于,回收接种装置产生的机械剥离非纤维素有机物碎片包括:通过固液分离装置从接种装置产生的废渣中分离得到碎片。The herb fiber biorefinery process waste residue treatment method according to claim 1, wherein the mechanically stripping the non-cellulosic organic material fragments produced by the recovery inoculating device comprises: separating the fragments from the waste residue generated by the inoculating device by the solid-liquid separation device.
  4. 根据权利要求1所述的草本纤维生物精制工艺废渣治理方法,其特征在于,所述方法还包括对磨细后的粉末进行筛选。The method according to claim 1, wherein the method further comprises screening the ground powder.
  5. 根据权利要求4所述的草本纤维生物精制工艺废渣治理方法,其特征在于,将筛选过程中截留的粗粉再次磨细。The herb fiber biorefinery process waste residue treatment method according to claim 4, wherein the coarse powder retained in the screening process is ground again.
  6. 根据权利要求4所述的草本纤维生物精制工艺废渣治理方法,其特征在于,通过筛选的粉末颗粒直径小于或者等于50μm。The herb fiber biorefinery process waste residue treatment method according to claim 4, wherein the diameter of the powder particles to be screened is less than or equal to 50 μm.
  7. 根据权利要求1所述的草本纤维生物精制工艺废渣治理方法,其特征在于,所述方法还包括对磨细后的粉末进行打包。The method according to claim 1, wherein the method further comprises packaging the ground powder.
  8. 根据权利要求1-7中任一项所述的草本纤维生物精制工艺废渣治理方法,其特征在于,所述治理方法还包括废汽治理的步骤,所述废汽是指草本纤维生物精制工艺过程中烘干装置加热烘干精制纤维所形成而又必须及时排出的蒸汽。The method for treating a waste residue of a herb fiber biorefinery process according to any one of claims 1 to 7, wherein the treatment method further comprises the step of treating waste steam, and the waste steam refers to a process of bioremediation of the herb fiber The medium drying device heats and dries the steam which is formed by the refined fiber and must be discharged in time.
  9. 根据权利要求8所述的草本纤维生物精制工艺废渣治理方法,其特征在于,将从烘干装置抽取的蒸汽输送至发酵装置,直接雾化可提高发酵装置内的温度和湿度。The herb fiber biorefinery process waste residue treatment method according to claim 8, wherein the steam extracted from the drying device is sent to the fermentation device, and the direct atomization can increase the temperature and humidity in the fermentation device.
  10. 根据权利要求8所述的草本纤维生物精制工艺废渣治理方法,其特征在于,将从烘干装置抽取的蒸汽输送至灭活装置和/或渍油装置内提高灭活装置和/或渍油装置内的温度。The herb fiber biorefining process waste residue treatment method according to claim 8, characterized in that the steam extracted from the drying device is sent to the inactivation device and/or the oil staining device to improve the inactivation device and/or the oil staining device. The temperature inside.
  11. 根据权利要求1-7中任一项所述的草本纤维生物精制工艺废渣治理方法,其特征在于,将从烘干装置抽取的蒸汽输送至乳化油调配槽和/或热水储存槽内。The herb fiber biorefining process waste residue treating method according to any one of claims 1 to 7, characterized in that the steam extracted from the drying device is sent to the emulsified oil blending tank and/or the hot water storage tank.
  12. 根据权利要求11所述的草本纤维生物精制工艺废渣治理方法,其特征在于,蒸汽的压力使其穿过高度大于或等于1000mm的液体或水层以达到水蒸汽所含热量最大限度的回收利用。The method for treating a waste residue of a herb fiber biorefining process according to claim 11, wherein the pressure of the steam passes through a liquid or water layer having a height greater than or equal to 1000 mm to achieve maximum recycling of heat contained in the water vapor.
  13. 一种草本纤维生物精制工艺废渣治理设备,其特征在于,所述设备包括:A herb fiber biorefinery process waste residue treatment device, characterized in that the device comprises:
    收集装置,包括罩在规范整理装置、烘干装置和开松装置外部收集机械剥离非纤维素有机物碎片的收尘壳体、对所述收尘壳体施加负压的抽提装置和与接种装置连接的固液分离装置,所述固液分离装置从接种装置产生的废液中分离得到碎片;The collecting device comprises a dust collecting shell covering the non-cellulosic organic matter pieces mechanically separated outside the standard finishing device, the drying device and the opening device, an extracting device applying a negative pressure to the dust collecting shell, and an inoculating device a solid-liquid separation device connected, the solid-liquid separation device separating the debris from the waste liquid generated by the inoculating device;
    除尘装置,包括与所述抽提装置连接以接收来自所述抽提装置的碎片的除尘壳体,所述除尘装置捕获并将碎片集中在一起;a dust removing device comprising a dust removing housing coupled to the extracting device to receive debris from the extracting device, the dust removing device capturing and collecting debris together;
    储存装置,用来接收并储存除尘装置集中的碎片及固液分离装置输送来的碎片;a storage device for receiving and storing debris collected in the dust removal device and debris transported by the solid-liquid separation device;
    运输装置,一端与所述储存装置连接;a transport device having one end connected to the storage device;
    磨粉装置,所述磨粉装置接收所述运输装置运来的碎片并对其进行磨细;a milling device that receives debris from the transport device and grinds it;
    分样筛,对磨粉装置磨细的粉末进行筛选使细粉通过筛眼落下同时使粗粉留在分样筛上;Separating the sieve, screening the finely ground powder of the grinding device to make the fine powder fall through the sieve eye while leaving the coarse powder on the sample sieve;
    截留装置,分样筛和磨粉装置连接将分样筛上的粗粉输送至磨粉装置再次磨细;The intercepting device, the sample sieve and the grinding device are connected, and the coarse powder on the sample sieve is transported to the grinding device to be ground again;
    打包装置,对磨细的粉末进行打包。A packing device that packs the ground powder.
  14. 根据权利要求13所述的草本纤维生物精制工艺废渣治理设备,其特征在于,所述收尘壳体包括罩在所述规范整理装置外部的第一壳体、罩在所述烘干装置外部的第二壳体和罩在所述开松装置外部的第三壳体,所述第一壳体、第二壳体和第三壳体的底壁均呈漏斗状,所述漏斗状的底部设有出尘口。The herb fiber biorefining process waste residue treating apparatus according to claim 13, wherein the dust collecting casing comprises a first casing covered outside the specification finishing device, and a cover outside the drying device a second casing and a third casing covering the outside of the opening device, wherein the bottom walls of the first casing, the second casing and the third casing are funnel-shaped, and the funnel-shaped bottom is provided There is a dust outlet.
  15. 根据权利要求14所述的草本纤维生物精制工艺废渣治理设备,其特征在于,所述第一壳体、第二壳体和第三壳体均具有允许制作草本纤维的原料输入壳体内的进料口和允许制作草本纤维的原料输出壳体外的出料口,所述进料口的高度小于或等于50mm,出料口的高度小于或等于40mm。The herb fiber biorefining process waste residue treating apparatus according to claim 14, wherein the first casing, the second casing and the third casing each have a raw material which allows the preparation of the raw material of the herbal fiber into the casing. The mouth and the material for allowing the preparation of the herbal fiber are outputted outside the casing, the height of the inlet is less than or equal to 50 mm, and the height of the outlet is less than or equal to 40 mm.
  16. 根据权利要求13所述的草本纤维生物精制工艺废渣治理设备,其特征在于,所述抽提装置为旋片式抽风机。The herb fiber biorefining process waste residue treating apparatus according to claim 13, wherein the extracting device is a rotary vane type exhaust fan.
  17. 根据权利要求13所述的草本纤维生物精制工艺废渣治理设备,其特征在于,所述除尘装置为水膜除尘装置,包括向所述除尘壳体内喷雾以形成扑捉碎片颗粒的水膜的水雾喷头,所述除尘壳体的底壁形成倾斜导流板使被水膜集中的碎片依靠重力移动至所述储存装置内。The herb fiber biorefining process waste residue treating apparatus according to claim 13, wherein the dust removing device is a water film dust removing device, and comprises a water mist sprayed into the dust removing casing to form a water film for capturing debris particles. The nozzle, the bottom wall of the dust removing housing forms a slanted baffle such that debris concentrated by the water film moves by gravity into the storage device.
  18. 根据权利要求13所述的草本纤维生物精制工艺废渣治理设备,其特征在于,所述储存装置的壳体的底壁形成倾斜导流板使碎片依靠重力移动至所述运输装置上。The herb fiber biorefining process waste residue treating apparatus according to claim 13, wherein the bottom wall of the casing of the storage device forms an inclined baffle to move the debris to the transport device by gravity.
  19. 根据权利要求13所述的草本纤维生物精制工艺废渣治理设备,其特征在于,所述分样筛包括筛体和驱动所述筛体震动的高频震动装置,所述筛体一端与磨粉装置连接接收磨细的粉末,另一端形成收缩出料口,使留在所述筛体上的粗粉经由所述出料口输出并输送至磨粉装置。The herb fiber bio-refining process waste residue treatment device according to claim 13, wherein the sample sieve comprises a sieve body and a high-frequency vibration device for driving the vibration of the sieve body, and one end of the sieve body and the grinding device The connection receives the ground powder and the other end forms a shrink-out spout, so that the coarse powder remaining on the screen is output through the discharge port and sent to the milling device.
  20. 根据权利要求13所述的草本纤维生物精制工艺废渣治理设备,其特征在于,所述分样筛的筛孔大于或等于300目。The herb fiber bioremediation process waste residue treatment apparatus according to claim 13, wherein the sieve hole of the sample sieve is greater than or equal to 300 mesh.
  21. 根据权利要求13-20中任一项所述的草本纤维生物精制工艺废渣治理设备,其特征在于,包括从烘干装置抽取蒸汽输送至发酵装置和/或灭活装置和/或渍油装置和/或乳化油调配槽和/或热水储存槽的管道。The herb fiber biorefining process waste residue treating apparatus according to any one of claims 13 to 20, characterized in that it comprises extracting steam from the drying device to the fermentation device and/or the inactivation device and/or the oil staining device and / or emulsified oil blending tank and / or hot water storage tank pipe.
  22. 根据权利要求21所述的草本纤维生物精制工艺废渣治理设备,其特征在于,将抽取的蒸汽以喷雾的形式进入所述发酵装置的壳体内增加发酵装置内的温度和湿度。The herb fiber biorefining process waste residue treating apparatus according to claim 21, wherein the extracted steam is introduced into the casing of the fermentation apparatus in the form of a spray to increase the temperature and humidity in the fermentation apparatus.
  23. 根据权利要求21述的草本纤维生物精制工艺废渣治理设备,其特征在于,将蒸汽输送至乳化油调配槽、热水储存槽内的输送管道伸入乳化油、水的液面下释放蒸汽且释放的蒸汽穿过高度大于或等于1000mm的液体、水层。The herb fiber bio-refining process waste residue treating apparatus according to claim 21, wherein the steam is transported to the emulsified oil mixing tank, and the conveying pipe in the hot water storage tank is extended into the emulsified oil, and the water is released under the surface of the water and released. The steam passes through a liquid or water layer having a height greater than or equal to 1000 mm.
  24. 根据权利要求21所述的草本纤维生物精制工艺废渣治理设备,其特征在于,所述管道包括连接烘干装置与热水储存槽的主管道、连接主管道与发酵装置的第一分管道、连接主管道与灭活装置的第二分管道、连接主管道与乳化油调配槽的第三分管道、连接主管道与渍油装置的第四分管道,所述主管道上设置有鼓风装置。The herb fiber biorefining process waste residue treating apparatus according to claim 21, wherein the pipe comprises a main pipe connecting the drying device and the hot water storage tank, a first branch pipe connecting the main pipe and the fermentation device, and the connection a second branch pipe of the main pipe and the inactivation device, a third branch pipe connecting the main pipe and the emulsified oil blending tank, a fourth branch pipe connecting the main pipe and the oil slick device, and the main pipe is provided with an air blowing device.
  25. 根据权利要求24所述的草本纤维生物精制工艺废渣治理设备,其特征在于,所述主管道靠近所述热水储存槽的一端设有压力控制阀,当主管道内蒸汽压力达到压力控制阀的控制压力时,所述压力控制阀开启,当蒸汽压力小于控制压力时,所述压力控制阀关闭。The herb fiber biorefining process waste residue treating apparatus according to claim 24, wherein a pressure control valve is disposed at one end of the main pipe near the hot water storage tank, and when the steam pressure in the main pipe reaches the control of the pressure control valve The pressure control valve is opened when pressure is applied, and the pressure control valve is closed when the steam pressure is less than the control pressure.
  26. 根据权利要求24所述的草本纤维生物精制工艺废渣治理设备,其特征在于,所述第一分管道、第二分管道、第三分管道和第四分管道分别设有分管道阀门。The herb fiber biorefining process waste residue treatment device according to claim 24, wherein the first sub-pipe, the second sub-pipe, the third sub-pipe and the fourth sub-pipe are respectively provided with a sub-pipe valve.
PCT/CN2018/086421 2017-09-18 2018-05-11 Treatment method and equipment for waste residues in herbaceous fiber biological refining process WO2019052205A1 (en)

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