CN204981708U - Separator that industrialization of glossy ganoderma spore polysaccharide was drawed - Google Patents
Separator that industrialization of glossy ganoderma spore polysaccharide was drawed Download PDFInfo
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Abstract
一种灵芝孢子多糖的产业化提取的分离装置,它是由提取罐、卧螺式离心机、卧螺式储液罐、卧螺式储渣罐、蝶式离心机、蝶式粉渣储罐、浓缩装置组成,提取罐与卧螺式离心机通过管道相接,卧螺式离心机分离出的液相进入卧螺式储液罐,沉渣进入卧螺式储渣罐,卧螺式储液罐与蝶式离心机相接,蝶式离心机分离出的粉渣进入蝶式粉渣储罐,液相进入浓缩装置,卧螺式储渣罐、蝶式粉渣储罐分别与提取罐相接。本实用新型装置简单,紧凑,机械化程度高,能有效地将孢子粉渣从灵芝孢子水提取液中除去,实现固液分离,获得高纯度高得率的灵芝孢子多糖,耗时短,减轻了劳动强度,适用于灵芝孢子多糖的工业化大生产。
A separation device for industrialized extraction of Ganoderma lucidum spore polysaccharide, which is composed of extraction tank, decanter centrifuge, decanter liquid storage tank, decanter slag storage tank, butterfly centrifuge, butterfly powder slag storage tank , concentration device, the extraction tank is connected to the decanter centrifuge through a pipeline, the liquid phase separated by the decanter centrifuge enters the decanter liquid storage tank, the sediment enters the decanter slag storage tank, and the decanter liquid storage The tank is connected with the butterfly centrifuge. The powder slag separated by the butterfly centrifuge enters the butterfly powder slag storage tank, and the liquid phase enters the concentration device. catch. The device of the utility model is simple, compact and highly mechanized, and can effectively remove the spore powder residue from the ganoderma spore water extract, realize solid-liquid separation, and obtain high-purity and high-yield ganoderma spore polysaccharides. The labor intensity is suitable for the industrialized large-scale production of the ganoderma lucidum spore polysaccharide.
Description
技术领域 technical field
本实用新型属于食用菌深加工技术领域,具体涉及一种灵芝孢子多糖的产业化提取分离方法。 The utility model belongs to the technical field of edible fungus deep processing, in particular to an industrial extraction and separation method of ganoderma lucidum spore polysaccharide.
背景技术 Background technique
灵芝(Ganodermalucidum)为多孔菌科灵芝属真菌,含有丰富的营养物质,在中国民间有着源远的食用历史,是一种具有补中益气、扶正固本功效的珍贵药材。灵芝孢子是灵芝生长成熟期,从灵芝菌褶中弹射出来的极其微小的卵形生殖细胞,呈椭圆形,短径平均8μm、长径平均11μm。现代科学研究表明,灵芝孢子比灵芝子实体有更强的生理活性,其中起主要作用的是灵芝孢子多糖,其具有多种生物活性,如抑制肿瘤、提高机体免疫力、提高机体耐缺氧能力、消除自由基等。 Ganoderma lucidum (Ganodermalucidum) is a fungus of the genus Ganoderma lucidum in the Polyporaceae family. It is rich in nutrients and has a long history of consumption in China. Ganoderma lucidum spores are extremely tiny oval germ cells ejected from the gills of Ganoderma lucidum in the mature stage of growth. They are oval in shape, with an average short diameter of 8 μm and an average long diameter of 11 μm. Modern scientific research shows that Ganoderma lucidum spores have stronger physiological activities than Ganoderma lucidum fruiting bodies, and the main role is Ganoderma lucidum spore polysaccharide, which has various biological activities, such as inhibiting tumors, improving the body's immunity, and improving the body's ability to withstand hypoxia , eliminate free radicals, etc.
然而,在对灵芝孢子的生物活性进行深入研究时,发现用水提取灵芝孢子多糖时,水提取液中的孢子粉渣过滤除去是件棘手的难题。由于灵芝孢子的粒径微小,平均只有10μm左右,600目的高密度的过滤筛网它也能透过,密度更高更细的过滤筛网虽然透过少,但是过滤速度非常慢,只适用于少量的实验室使用,难于实现产业化。 However, in the in-depth study of the biological activity of Ganoderma lucidum spores, it was found that when extracting the polysaccharides of Ganoderma lucidum spores with water, it is a thorny problem to filter and remove the spore powder residue in the water extract. Because the particle size of Ganoderma lucidum spores is small, with an average of only about 10 μm, it can also pass through a 600-mesh high-density filter screen. Although a higher-density and finer filter screen passes through less, the filtration speed is very slow, and it is only suitable for A small amount of laboratory use is difficult to achieve industrialization.
目前产业化的通常处理方法是,提取液采用静置分层、虹吸上清液、400-500目滤布“过筛法”仅能去除60-70%的灵芝孢子粉渣。由于提取液中孢子粉渣的密度与上清液相近,沉降很慢,通常需要静置过夜,但是仍然还不能将上清液与孢子粉渣有效分开,上清液占总体积比例仅60%,而且漫长的沉降时间,还会导致灵芝孢子吸水发酵产生酸败,失去利用价值。由于常规方法耗时太长,操作过程繁琐,通常只提取一次,提取率大约为62%,提取率低资源的利用率也低。耗时长,操作繁琐,难以实现产业化生产,成为灵芝孢子多糖产业化开发利用的瓶颈。 The usual processing method for industrialization at present is that the extraction solution adopts static stratification, siphon supernatant, and 400-500 mesh filter cloth "sieving method" can only remove 60-70% of the ganoderma lucidum spore powder residue. Because the density of the spore powder and residue in the extract is close to that of the supernatant, the sedimentation is very slow, and it usually needs to be left standing overnight. However, the supernatant and the spore powder can not be effectively separated, and the supernatant accounts for only 60% of the total volume. %, and the long settling time will also cause the ganoderma lucidum spores to absorb water and ferment to produce rancidity and lose their utilization value. Because the conventional method takes too long and the operation process is cumbersome, it is usually only extracted once, and the extraction rate is about 62%. The extraction rate is low and the utilization rate of resources is also low. It takes a long time, the operation is cumbersome, and it is difficult to realize industrial production, which has become a bottleneck for the industrial development and utilization of Ganoderma lucidum spore polysaccharide.
在现有的公开技术中,专利CN101703531B“一种灵芝孢子粉的冷冻真空干燥和提纯的方法”,采用80-500目的绢布、棉布、纱布或不锈钢筛进行过滤,滤液再用1-30μm孔径滤膜的空气压滤器进行压滤。该方法需要不断地更换清洗滤布、不能自动化操作,劳动强度大,滤膜耗材多,只合适实验室小试。专利CN102766593A“一种灵芝孢子的提纯方法”,是将灵芝孢子粉混合液通过螺旋分离器后,用大于300目的滤网过滤,滤液再装入滤粉袋,由空压机将滤粉袋中水压出,由于滤粉袋易被堵塞,也需要不断地清洗或更换该方法不仅工序步骤复杂,也不能自动化操作,难以实现产业化生产。 In the existing public technology, the patent CN101703531B "a method for freeze-drying and purifying Ganoderma lucidum spore powder" uses 80-500 mesh silk cloth, cotton cloth, gauze or stainless steel sieve to filter, and the filtrate is then filtered with a pore size of 1-30 μm Air filter with filter membrane for pressure filtration. This method needs to constantly replace and clean the filter cloth, cannot be operated automatically, is labor-intensive, and has a lot of filter membrane consumables, so it is only suitable for small laboratory tests. Patent CN102766593A "a purification method of Ganoderma lucidum spores" is to pass the mixed liquid of Ganoderma lucidum spore powder through a spiral separator, filter it with a filter screen larger than 300 mesh, put the filtrate into a filter bag, and put it into the filter bag by an air compressor. If the water is pressed out, since the powder filter bag is easy to be blocked, it needs to be continuously cleaned or replaced. This method is not only complicated in process steps, but also cannot be operated automatically, and it is difficult to realize industrial production.
如果采用传统的板框压滤机进行分离,因水提取液中的孢子粉渣粘度高,质地软,随着过滤的进行,逐渐聚集在滤布上,导致滤布堵塞,过滤速度减慢,耗时増长(约10-12hr)、且更换滤布繁琐,因此此法也不可行。有人采用管式离心机进行分离,由于灵芝孢子粉水提取混悬液中固形物含量较高,管式离心机转鼓容积小,物料进入转鼓后,短时间内大量沉淀沉积在转鼓上,需要频繁停机拆卸转鼓进行除渣,增加了操作的复杂性,影响生产效率。此外,沉淀较粘,清洗时比较困难。因此,管式离心机处理能力和自动化程度都比较差。 If a traditional plate and frame filter press is used for separation, because the spore powder residue in the water extract has high viscosity and soft texture, as the filtration progresses, it will gradually gather on the filter cloth, causing the filter cloth to be clogged and the filtration speed to slow down. Time-consuming growth (about 10-12hr), and changing filter cloth is loaded down with trivial details, so this method is also not feasible. Some people use a tubular centrifuge for separation. Due to the high content of solids in the water extraction suspension of Ganoderma lucidum spore powder, the volume of the drum of the tubular centrifuge is small, and after the material enters the drum, a large amount of sediment is deposited on the drum in a short time , it is necessary to stop frequently to disassemble the drum for slag removal, which increases the complexity of the operation and affects the production efficiency. In addition, the sediment is sticky and difficult to clean. Therefore, the processing capacity and degree of automation of the tube centrifuge are relatively poor.
发明内容 Contents of the invention
本实用新型的目的在于针对目前由于灵芝孢子极其微小,用水提取灵芝孢子多糖时固液难以过滤分离,致使工业化生产效率低的缺点,提供一种可工业化生产、提取效率高的灵芝孢子多糖产业化提取的分离装置。 The purpose of this utility model is to provide a Ganoderma lucidum spore polysaccharide industrialization that can be industrialized and has high extraction efficiency in view of the current disadvantages that the Ganoderma lucidum spore polysaccharide is extremely small, and it is difficult to filter and separate the solid and liquid when extracting the Ganoderma lucidum spore polysaccharide with water, resulting in low industrial production efficiency. Extraction of the separation device.
本实用新型所采用的技术方案为一种灵芝孢子多糖的产业化提取分离的装置,它是由提取罐、卧螺式离心机、卧螺式储液罐、卧螺式储渣罐、蝶式离心机、蝶式粉渣储罐、浓缩装置组成,提取罐与卧螺式离心机通过管道相接,卧螺式离心机分离出的液相进入卧螺式储液罐,沉渣进入卧螺式储渣罐,卧螺式储液罐与蝶式离心机相接,蝶式离心机分离出的粉渣进入蝶式粉渣储罐,液相进入浓缩装置,卧螺式储渣罐、蝶式粉渣储罐分别与提取罐相接。 The technical scheme adopted by the utility model is a device for industrialized extraction and separation of Ganoderma lucidum spore polysaccharide, which is composed of an extraction tank, a horizontal screw centrifuge, a horizontal screw type liquid storage tank, a horizontal screw type slag storage tank, a butterfly type It consists of a centrifuge, a butterfly powder slag storage tank and a concentration device. The extraction tank is connected to the decanter centrifuge through a pipeline. The liquid phase separated by the decanter centrifuge enters the decanter liquid storage tank, and the sediment enters the decanter centrifuge. The slag storage tank, the horizontal screw liquid storage tank is connected with the butterfly centrifuge, the powder slag separated by the butterfly centrifuge enters the butterfly powder slag storage tank, and the liquid phase enters the concentration device, the horizontal screw slag storage tank, the butterfly centrifuge The powder slag storage tanks are respectively connected with the extraction tanks.
所述的卧螺式储渣罐、蝶式粉渣储罐分别与提取罐相接。是指通过输送管等连接,出渣可通过机械将卧螺式储渣罐、碟式粉渣储罐的内容物输送入提取罐。 The horizontal screw type slag storage tank and the butterfly powder slag storage tank are respectively connected with the extraction tank. It means that the contents of the horizontal screw type slag storage tank and the dish type powder slag storage tank can be transported into the extraction tank through mechanical connection through the transfer pipe.
将灵芝孢子放入提取罐提取后,提取液直接进入卧螺式离心机进行分离,所得的液相进入卧螺式储液罐(由于两个离心机的速度不一样,所以需要有个卧螺式储液罐进行储液缓冲,若二者速度可达一致,可直接连接),沉渣进入卧螺式储渣罐,卧螺式储液罐与蝶式离心机相接,蝶式离心机分离出的粉渣进入蝶式粉渣储罐,液相进入浓缩装置,到全部分离完后,再将卧螺式储渣罐和蝶式粉渣储罐内的渣放入提取罐进行二次提取。 After the Ganoderma lucidum spores are put into the extraction tank for extraction, the extract directly enters the decanter centrifuge for separation, and the obtained liquid phase enters the decanter liquid storage tank (because the speeds of the two centrifuges are different, a decanter centrifuge is required. Type liquid storage tank for liquid storage and buffering, if the two speeds can reach the same level, they can be directly connected), the sediment enters the horizontal screw type storage tank, the horizontal screw type liquid storage tank is connected with the butterfly centrifuge, and the butterfly centrifuge separates The discharged powder and slag enters the butterfly powder and slag storage tank, and the liquid phase enters the concentration device. After all the separation is completed, the slag in the horizontal screw-type slag storage tank and butterfly powder and slag storage tank is put into the extraction tank for secondary extraction. .
本实用新型利用两种不同的分离装置对孢子粉的水提取液进行固液分离,卧螺离心机的转鼓与螺旋以一定差速同向高速旋转,将机内灵芝孢子水提取混悬液,在高速旋转的离心力场作用下,较重的孢子粉固相沉积在转鼓内壁形成沉淀的粉渣,被旋转的螺旋连续不断地推到转鼓的锥端,经排渣口排出。较轻的微混悬液相(内含10-20%粉渣)则形成内层液环,由转鼓大端溢流口连续溢出转鼓,经排液口排出,从而实现固相与微混悬液相分离。 The utility model uses two different separation devices to separate the water extract of spore powder from solid to liquid. The drum and the screw of the decanter centrifuge rotate at a high speed in the same direction at a certain differential speed, and the water extract suspension of Ganoderma lucidum spores in the machine is extracted. , under the action of the high-speed rotating centrifugal force field, the heavy spore powder solid-phase deposits on the inner wall of the drum to form precipitated powder slag, which is continuously pushed to the cone end of the drum by the rotating screw and discharged through the slag discharge port. The lighter microsuspension liquid phase (containing 10-20% powder slag) forms an inner liquid ring, which continuously overflows the drum from the overflow port at the large end of the drum, and is discharged through the liquid discharge port, so as to realize solid phase and micro-suspension. The suspension phase separated.
蝶式分离机适合分离含固量低的混悬液,它是通过电驱动碟式转鼓绕主轴线做高速回转,当卧螺离心机分离出的微混悬液由上部中心加料管流至转鼓底部时,再经碟片下座面的分流孔趋向转鼓壁,在离心力场作用下,比重大的孢子粉流向转鼓内壁形成沉渣,经出渣口排出,分离出液相则沿锥形碟片的外锥面向轴心流动,到上部经液相出口排出,实现固相和液相的分离。 The butterfly separator is suitable for separating suspensions with low solid content. It rotates the disc drum around the main axis at high speed through electric drive. When the microsuspension separated by the decanter centrifuge flows from the upper central feeding pipe to the At the bottom of the drum, it goes to the wall of the drum through the diversion hole on the lower surface of the disc. Under the action of the centrifugal force field, the spore powder with a large specific gravity flows to the inner wall of the drum to form sediment, which is discharged through the slag outlet, and the liquid phase is separated along the The outer cone of the conical disc flows towards the axis, and the upper part is discharged through the liquid phase outlet to realize the separation of solid phase and liquid phase.
本实用新型经过卧螺式离心机分离后,灵芝孢子水提取液中80-90%的固相粉渣被分离排出。分离出的微混悬液相,再利用蝶式离心机进行分离,所获得的上液相浊度低(大约100ntu)、近于清澈。由于上述分离的时间较短,一般240kg的脱脂孢子粉,其水提取液大约是2.4T,固液分离的时间为1.5小时,时间短,所以可以继续进行二次提取使提取率由现有的62%提高到90%。上述两机串联循环使用,将灵芝孢子的水提取混悬液实现固液分离,由于能实现自动进料自动出料的在线连续自动化操作,适合制备灵芝孢子多糖的产业化大生产的需要。 In the utility model, after being separated by a horizontal screw centrifuge, 80-90% of the solid-phase powder residue in the ganoderma lucidum spore water extract is separated and discharged. The separated microsuspension phase is separated by a butterfly centrifuge, and the obtained upper liquid phase has low turbidity (about 100ntu) and is almost clear. Because the time of above-mentioned separation is shorter, generally 240kg defatted spore powder, its water extract liquid is about 2.4T, and the time of solid-liquid separation is 1.5 hours, and the time is short, so can continue to carry out secondary extraction to make extraction rate by existing 62% increased to 90%. The above two machines are used in series and recycled to separate the water-extracted suspension of Ganoderma lucidum spores to achieve solid-liquid separation. Since the online continuous automatic operation of automatic feeding and automatic discharging can be realized, it is suitable for the needs of industrialized large-scale production of polysaccharides prepared from Ganoderma lucidum spores.
对上述设备进行进一步的设定: Make further settings on the above devices:
所述的卧螺式离心机的转速3800r/min---5000r/min,分离因数2870-3530;蝶式离心机的转鼓转速7000r/min--7600r/min,分离因数10000-11200。 The rotating speed of the decanter centrifuge is 3800r/min---5000r/min, and the separation factor is 2870-3530; the drum rotating speed of the butterfly centrifuge is 7000r/min--7600r/min, and the separation factor is 10000-11200.
本申请人经过无数次的反复实验,当设备达到上述条件时固液分离的效果最好。 After numerous repeated experiments by the applicant, the effect of solid-liquid separation is the best when the equipment reaches the above conditions.
本实用新型的有益效果为:将灵芝孢子水提取液的固液分离实现自动化,既能连续进料、又能连续出料,24小时连续产业化作业。操作简便、分离速度快,缩短了孢子在水提取液中浸泡的时间,有效地避免发生发酵酸败作用,很好地保持灵芝孢子粉原有的芳香风味。本实用新型将传统常规一次提取的分离出的粉渣,再输送到提取罐,进行二次自动化提取,减少了传统分离的人工操作、步骤多造成的损失,二次提取提高了多糖得率,二次提取的总得率为90%,比传统的一次提取提高了45%,这不仅提高了附加值,而且提高了天然资源的利用率。本实用新型的装置简单,紧凑,机械化程度高。 The beneficial effect of the utility model is that the solid-liquid separation of the water extract of ganoderma lucidum spores is automated, the material can be fed continuously and the material can be discharged continuously, and the industrial operation can be carried out continuously for 24 hours. The operation is simple and the separation speed is fast, the time for soaking the spores in the water extract is shortened, the fermentation and rancidity can be effectively avoided, and the original aromatic flavor of the ganoderma lucidum spore powder can be well maintained. The utility model transports the powder slag separated from the conventional primary extraction to the extraction tank for secondary automatic extraction, which reduces the loss caused by traditional manual operations and multiple steps of separation, and the secondary extraction improves the yield of polysaccharides. The total yield of the secondary extraction is 90%, which is 45% higher than the traditional primary extraction, which not only increases the added value, but also improves the utilization rate of natural resources. The device of the utility model is simple, compact and has a high degree of mechanization.
附图说明 Description of drawings
图1为本实用新型灵芝孢子多糖的水提取装置图 Fig. 1 is the water extraction device figure of the utility model Ganoderma lucidum spore polysaccharide
其中1提取罐2卧螺式离心机3卧螺式储液罐4卧螺式储渣罐5蝶式离心机6蝶式粉渣储罐7排放口8浓缩装置。 Among them, 1 extraction tank, 2 horizontal screw centrifuges, 3 horizontal screw liquid storage tanks, 4 horizontal screw slag storage tanks, 5 butterfly centrifuges, 6 butterfly powder slag storage tanks, 7 discharge ports, and 8 concentration devices.
具体实施方式 detailed description
下面的实施例可以使本专业的技术人员更理解本实用新型,但不以任何形式限制本实用新型。 The following examples can make those skilled in the art better understand the utility model, but do not limit the utility model in any form.
如图1所示,一种灵芝孢子多糖的产业化提取分离的装置,它是由提取罐1、卧螺式离心机2、卧螺式储液罐3、卧螺式储渣罐4、蝶式离心机5、蝶式粉渣储罐6、浓缩装置8组成,提取罐1与卧螺式离心机2通过管道相接,卧螺式离心机2分离出的液相进入卧螺式储液罐3,沉渣进入卧螺式储渣罐4,卧螺式储液罐3与蝶式离心机5相接,蝶式离心机5分离出的粉渣进入蝶式粉渣储罐6,液相进入浓缩装置8,卧螺式储渣罐4、蝶式粉渣储罐6分别与提取罐1相接。所述的卧螺式储渣罐4、蝶式粉渣储罐6分别与提取罐1相接,这是为了二次提取的送料,主要是通过输送管等进行连接,或通过机械将卧螺式储渣罐4、碟式粉渣储罐6的内容物输送入提取罐1,卧螺式储渣罐4和蝶式粉渣储罐6的出口接有三通,一个与本罐体连接,另一个口与提取罐1连接,还有一个为排放口7,第二次提取后沉渣从排放口7排出。 As shown in Figure 1, a kind of device of the industrialized extraction and separation of Ganoderma lucidum spore polysaccharide, it is made of extraction tank 1, decanter centrifuge 2, decanter liquid storage tank 3, decanter slag storage tank 4, butterfly The extraction tank 1 is connected to the decanter centrifuge 2 through pipelines, and the liquid phase separated by the decanter centrifuge 2 enters the decanter liquid storage Tank 3, the sediment enters the horizontal screw type slag storage tank 4, the horizontal screw type liquid storage tank 3 is connected with the butterfly centrifuge 5, and the powder slag separated by the butterfly centrifuge 5 enters the butterfly type powder slag storage tank 6, and the liquid phase Entering the concentration device 8, the horizontal screw type slag storage tank 4 and the butterfly powder slag storage tank 6 are respectively connected with the extraction tank 1. The horizontal screw-type slag storage tank 4 and the butterfly powder-slag storage tank 6 are respectively connected to the extraction tank 1. This is for the feeding of the secondary extraction, mainly through the delivery pipe, etc., or by mechanically connecting the horizontal screw type The contents of the type slag storage tank 4 and the dish type powder slag storage tank 6 are transported into the extraction tank 1, and the outlets of the horizontal screw type slag storage tank 4 and the butterfly powder slag storage tank 6 are connected with three links, one of which is connected with the tank body, The other port is connected with the extraction tank 1, and another is the discharge port 7, and the sediment is discharged from the discharge port 7 after the second extraction.
卧螺式离心机的转速2500-5000r/min,分离因数2300-3530;蝶式离心机的转鼓转速6000-7600r/min,分离因数9900-12800。 The rotation speed of the decanter centrifuge is 2500-5000r/min, and the separation factor is 2300-3530; the drum speed of the butterfly centrifuge is 6000-7600r/min, and the separation factor is 9900-12800.
实施例一:利用上述装置工业化提取分离灵芝孢子多糖:称取240kg脱脂孢子粉置于3.0T提取罐1中,加入8倍孢子粉量的水共1.92T,加热到100度,沸水提取,恒温搅拌提取2小时后,将上述孢子粉水提取混悬液通过卧螺式离心机2(转鼓转速3800r/min、分离因数2860)分离得卧螺固相粉渣和微混悬液相,分别储存于卧螺式储渣罐4和卧螺式储液罐3,由于两个离心机的速度不一样,所以需要有个卧螺式储液罐进行储液,若二者速度可达一致,可直接连接,卧螺式储液罐3内的微混悬液相进入蝶式离心机5(转鼓转速7600r/min、分离因数10000),分离得液相和沉渣,液相进入进入浓缩装置8,沉渣进入蝶式粉渣储罐6。待第一次提取分离结束后,将卧螺式储渣罐4和蝶式粉渣储罐6中的沉渣输送入提取罐1中重复第一次提取分离的步骤进行第二次提取,卧螺式储渣罐4和蝶式粉渣储罐6的出口接有三通,一端与罐体连接,另一端与提取罐1连接,还有一个为排放口7,第二次提取后沉渣从排放口排出,将卧螺式储渣罐4和蝶式粉渣储罐6中的沉渣废弃,最终将两次进入浓缩装置8的蝶式液相进行精制浓缩得到灵芝孢子粉多糖浸膏(多糖得率为9.8%,含量为15.4%)。液相取样进行实验分析,液相的浊度为114nut,比较清澈。 Example 1: Industrial extraction and separation of Ganoderma lucidum spore polysaccharides using the above-mentioned device: Weigh 240kg of defatted spore powder and place it in a 3.0T extraction tank 1, add 8 times the amount of water of the spore powder to a total of 1.92T, heat to 100 degrees, extract with boiling water, and keep the temperature constant After stirring and extracting for 2 hours, the above-mentioned spore powder water extraction suspension was separated by decanter centrifuge 2 (drum speed 3800r/min, separation factor 2860) to obtain decanter solid phase powder slag and microsuspension liquid phase, respectively It is stored in the horizontal screw type slag storage tank 4 and the horizontal screw type liquid storage tank 3. Since the speeds of the two centrifuges are different, a horizontal screw type liquid storage tank is required for liquid storage. If the speed of the two can reach the same, Can be directly connected, the microsuspension liquid phase in the horizontal screw type liquid storage tank 3 enters the butterfly centrifuge 5 (drum speed 7600r/min, separation factor 10000), separates the liquid phase and sediment, and the liquid phase enters the concentration device 8. The sediment enters the butterfly powder and residue storage tank 6. After the first extraction and separation is completed, the sediment in the horizontal screw type slag storage tank 4 and the butterfly powder residue storage tank 6 is transported into the extraction tank 1 to repeat the steps of the first extraction and separation for the second extraction. The outlets of the type slag storage tank 4 and the butterfly powder slag storage tank 6 are connected with a tee, one end is connected with the tank body, the other end is connected with the extraction tank 1, and the other is a discharge port 7. After the second extraction, the sediment is discharged from the discharge port. Discharge, the sediment in the horizontal screw type slag storage tank 4 and the butterfly powder slag storage tank 6 is discarded, and finally the butterfly liquid phase that enters the concentration device 8 twice is refined and concentrated to obtain the polysaccharide extract of Ganoderma lucidum spore powder (polysaccharide yield is 9.8%, and the content is 15.4%). The liquid phase was sampled for experimental analysis, and the turbidity of the liquid phase was 114nut, which was relatively clear.
实施例二:称取240kg脱脂孢子粉置于3.0T提取罐1中,加入10倍孢子粉量的水共2.4T作沸水提取,恒温搅拌提取2小时后,将上述孢子粉水提取混悬液依次通过卧螺式离心机(转鼓转速3800r/min、分离因数2860)、蝶式离心机(转鼓转速7600r/min、分离因数10000)串联系统循环分离液相与固相。最终浓缩得到灵芝孢子粉多糖浸膏(多糖得率为10.2%,含量为15.9%)。液相取样进行实验分析,液相的浊度为107nut,比较清澈。其余未述部分与上例相同。 Embodiment two: take by weighing 240kg degreasing spore powder and place in 3.0T extraction tank 1, add the water of 10 times of spore powder amount altogether 2.4T and make boiling water extraction, after stirring and extracting at constant temperature for 2 hours, extract the above-mentioned spore powder water suspension The liquid phase and the solid phase are separated by a decanter centrifuge (drum speed 3800r/min, separation factor 2860) and a butterfly centrifuge (drum speed 7600r/min, separation factor 10000) in series. Finally, the polysaccharide extract of Ganoderma lucidum spore powder was obtained by concentration (the polysaccharide yield was 10.2%, and the content was 15.9%). The liquid phase was sampled for experimental analysis, and the turbidity of the liquid phase was 107nut, which was relatively clear. Other unmentioned parts are the same as the above example.
实施例三:称取200kg脱脂孢子粉置于提取装置中,加入12倍孢子粉量的水共2.4T,作沸水提取,恒温搅拌提取2小时后,将上述孢子粉水提取混悬液依次通过卧螺式离心机(转鼓转速5000r/min、分离因数3525)、蝶式离心机(转鼓转速7060r/min、分离因数11200)串联系统循环分离液相与固相。浓缩得到灵芝孢子粉多糖浸膏(多糖得率为10.5%,含量为16%)。液相取样进行实验分析,液相的浊度为100nut,比较清澈。其余未述部分与实施例1相同。 Embodiment 3: Weigh 200kg of defatted spore powder and place it in the extraction device, add 12 times the amount of water of spore powder to a total of 2.4T for boiling water extraction, stir and extract at a constant temperature for 2 hours, pass the above-mentioned spore powder water extraction suspension successively through Decanter centrifuge (drum speed 5000r/min, separation factor 3525) and butterfly centrifuge (drum speed 7060r/min, separation factor 11200) are connected in series to separate liquid and solid phases. Concentrate to obtain Ganoderma lucidum spore powder polysaccharide extract (polysaccharide yield 10.5%, content 16%). The liquid phase was sampled for experimental analysis, and the turbidity of the liquid phase was 100nut, which was relatively clear. All the other undescribed parts are the same as in Example 1.
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| CN105175564A (en) * | 2015-08-21 | 2015-12-23 | 仙芝科技(福建)股份有限公司 | Industrial extraction and separation method of ganoderma spore polysaccharide and separation device |
| CN108936185A (en) * | 2018-08-28 | 2018-12-07 | 贵州宏财聚农投资有限责任公司 | A kind of roxburgh rose juice drink Normal juice pre-treating technology and separating and filtering device |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN105175564A (en) * | 2015-08-21 | 2015-12-23 | 仙芝科技(福建)股份有限公司 | Industrial extraction and separation method of ganoderma spore polysaccharide and separation device |
| CN105175564B (en) * | 2015-08-21 | 2018-01-16 | 仙芝科技(福建)股份有限公司 | The industrialization extraction separation method and separator of ganoderma spore polysaccharide |
| CN108936185A (en) * | 2018-08-28 | 2018-12-07 | 贵州宏财聚农投资有限责任公司 | A kind of roxburgh rose juice drink Normal juice pre-treating technology and separating and filtering device |
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