CN115777981A - Production method and device of reconstituted tobacco raw material extracting solution - Google Patents
Production method and device of reconstituted tobacco raw material extracting solutionDownload PDFInfo
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Abstract
Description
Translated fromChinese技术领域technical field
本发明涉及超重力萃取技术领域，特别涉及一种再造烟叶原料提取液的生产方法及装置。The invention relates to the technical field of high-gravity extraction, in particular to a production method and device for extracting liquid of reconstituted tobacco leaf raw materials.
背景技术Background technique
目前，世界上广泛被采纳的烟草薄片的生产方式主要有稠浆法、辊压法和造纸法。其中，造纸法是目前发展最迅速的烟草薄片的制备方法，通过造纸法制备的烟草薄片各项理化指标均优于稠浆法和辊压法得到的烟草薄片，因此越来越受到企业的青睐。At present, the production methods of tobacco sheets widely adopted in the world mainly include thick pulp method, roller pressing method and papermaking method. Among them, the papermaking method is currently the fastest-growing tobacco sheet preparation method. The physical and chemical indicators of the tobacco sheet prepared by the papermaking method are better than those obtained by the thick pulp method and the rolling method, so it is more and more favored by enterprises. .
造纸法生产烟草薄片一般是将烟梗提取后，烟梗用于制作薄片的制浆，但是烟梗液有三分之二不能利用，烟梗液中烟碱含量比较低，富集比较困难，并且由于烟梗液含有烟碱、色素等污水处理比较困难Tobacco flakes produced by the papermaking method are generally extracted from the tobacco stems, and the tobacco stems are used to make pulp for the flakes, but two-thirds of the tobacco stem liquid cannot be used, and the content of nicotine in the tobacco stem liquid is relatively low, making it difficult to enrich. And because the tobacco stem liquid contains nicotine, pigments and other sewage treatment is more difficult
因此，如何提供一种再造烟叶原料提取液的生产方法，不仅可以解决烟梗液难于处理的问题，还能够有效提高产品的提取率是本领域技术人员亟需解决的技术问题。Therefore, how to provide a production method for extracting liquid of reconstituted tobacco leaf raw materials, which can not only solve the problem of difficult handling of tobacco stem liquid, but also effectively improve the extraction rate of the product is a technical problem urgently needed by those skilled in the art.
发明内容Contents of the invention
有鉴于此，本发明的目的在于提供一种再造烟叶原料提取液的生产方法，不仅可以解决烟梗液难于处理的问题，还能够有效提高产品的提取率。In view of this, the object of the present invention is to provide a production method of extracting liquid of reconstituted tobacco leaf raw material, which can not only solve the problem that the tobacco stem liquid is difficult to handle, but also effectively improve the extraction rate of the product.
本发明的另一目的还在于提供一种再造烟叶原料提取液的生产装置。Another object of the present invention is to provide a production device for extracting liquid of reconstituted tobacco leaf raw material.
为实现上述目的，本发明提供如下技术方案：To achieve the above object, the present invention provides the following technical solutions:
一种再造烟叶原料提取液的生产方法，包括以下步骤：A method for producing reconstituted tobacco raw material extract, comprising the following steps:
S100：将烟叶或烟梗粉碎为烟草粉；S100: crushing tobacco leaves or tobacco stems into tobacco powder;
S200：将溶剂加入所述烟草粉内进行搅拌，直至搅拌成烟草桨，所述溶剂的温度为预设温度值；S200: adding a solvent into the tobacco powder and stirring until a tobacco paddle is formed, and the temperature of the solvent is a preset temperature value;
S300：将所述烟草桨输送至超重力设备中，对所述烟草桨中的有效物质进行提取；S300: transporting the tobacco paddle to a supergravity device, and extracting effective substances in the tobacco paddle;
S400：对提取后的所述烟草桨进行压滤，得到滤渣和滤液，所述滤渣用于制作再造烟叶，所述滤液用于再造烟叶涂布液使用。S400: Press-filter the extracted tobacco paddle to obtain a filter residue and a filtrate, the filter residue is used for making reconstituted tobacco leaves, and the filtrate is used for reconstituted tobacco leaf coating liquid.
优选的，所述步骤S100中，所述烟草粉为10目-200目。Preferably, in the step S100, the tobacco powder is 10-200 mesh.
优选的，所述步骤S200中，所述第一预设温度值为30℃-80℃。Preferably, in the step S200, the first preset temperature value is 30°C-80°C.
优选的，所述步骤S200中，所述溶剂的重量为所述烟草粉的重量的2-6倍。Preferably, in the step S200, the weight of the solvent is 2-6 times the weight of the tobacco powder.
优选的，所述步骤S200中，所述烟草粉与所述溶剂在原料罐中进行搅拌。Preferably, in the step S200, the tobacco powder and the solvent are stirred in a raw material tank.
优选的，所述步骤S300中，所述烟草桨进入所述超重力设备的进料速度为500kg-2000kg/h。Preferably, in the step S300, the feed rate of the tobacco paddle into the supergravity device is 500kg-2000kg/h.
优选的，所述步骤S300中，所述有效物质低于所述烟草桨中物质总量的10％。Preferably, in the step S300, the effective substance is less than 10% of the total substance in the tobacco paddle.
优选的，所述步骤S400中，通过所述压滤机对提取后的所述烟草桨进行压滤。Preferably, in the step S400, the extracted tobacco paddle is press-filtered by the filter press.
一种再造烟叶原料提取液的生产装置，应用于如上述任意一项所述的再造烟叶原料提取液的生产方法中，其特征在于，包括原料罐、第一输送泵、超重力设备、压滤机、加热浓缩罐、冷凝器、缓冲罐、第二输送泵和产品罐；A production device for reconstituted tobacco leaf raw material extract, which is applied to the production method of reconstituted tobacco leaf raw material extract as described in any one of the above, characterized in that it includes a raw material tank, a first delivery pump, supergravity equipment, a filter press Machine, heating concentration tank, condenser, buffer tank, second transfer pump and product tank;
所述原料罐通过所述第一输送泵与所述超重力设备的第一进料口相连通，所述超重力设备的第一出料口与所述压滤机的进料口相连通，所述压滤机的出料口与所述加热浓缩罐相连通，所述加热浓缩罐的出料口与所述超重力设备的第二进料口相连通，所述超重力设备的第二进料口与所述冷凝器的进料口相连通，所述冷凝器的出料口与所述缓冲罐的进料口相连通，所述缓冲罐的出料口通过所述第二输送泵与所述超重力设备的第三进料口相连通。The raw material tank communicates with the first feeding port of the supergravity equipment through the first transfer pump, and the first outlet of the supergravity equipment communicates with the feeding port of the filter press, The discharge port of the filter press is connected with the heating concentration tank, the discharge port of the heating concentration tank is connected with the second feeding port of the supergravity equipment, and the second feeding port of the supergravity device is The feed port is connected with the feed port of the condenser, the discharge port of the condenser is connected with the feed port of the buffer tank, and the discharge port of the buffer tank is passed through the second delivery pump It communicates with the third feeding port of the supergravity equipment.
优选的，所述冷凝器包括第一冷凝器和第二冷凝器，所述第一冷凝器的进料口与所述超重力设备的所述第二出料口相连通，所述第一冷凝器的出料口与所述第二冷凝器的进料口相连通，所述第二冷凝器的出料口与所述缓冲罐的进料口相连通。Preferably, the condenser includes a first condenser and a second condenser, the feed port of the first condenser communicates with the second discharge port of the supergravity equipment, and the first condenser The discharge port of the condenser is connected with the feed port of the second condenser, and the discharge port of the second condenser is connected with the feed port of the buffer tank.
由以上技术方案可以看出，和现有技术相比，采用本发明实施例所公开的再造烟叶原料提取液的生产方法，对烟草中有效物质的提取率能够超过90％，提取效率提高了，溶剂用量降低了2-5倍，减少了能耗，提高了效益，降低了提取的时间，减少了果胶和色素的提取量，绿色环保，得到的烟草提取液可以完全适用于再造烟叶，不产生二次污染。It can be seen from the above technical solutions that compared with the prior art, the extraction rate of effective substances in tobacco can exceed 90% by adopting the production method of the raw material extract of reconstituted tobacco leaf disclosed in the embodiment of the present invention, and the extraction efficiency is improved. The amount of solvent is reduced by 2-5 times, energy consumption is reduced, benefit is improved, extraction time is reduced, pectin and pigment extraction amount are reduced, it is green and environmentally friendly, and the obtained tobacco extract can be completely applied to reconstituted tobacco leaves without produce secondary pollution.
附图说明Description of drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案，下面对实施例或现有技术描述中所需要使用的附图作简单地介绍，显而易见的，下面描述中的附图仅仅是本发明的实施例，对于本领域普通技术人员来讲，在不付出创造性劳动的前提下，还可以根据提供的附图获得其他的附图。In order to more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the following briefly introduces the drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description are only It is an embodiment of the present invention, and those skilled in the art can also obtain other drawings according to the provided drawings without creative work.
图1为本发明实施例所公开的再造烟叶原料提取液的生产方法的流程示意图；Fig. 1 is a schematic flow diagram of the production method of the reconstituted tobacco raw material extract disclosed in the embodiment of the present invention;
图2为本发明实施例所公开的再造烟叶原料提取液的生产装置的结构示意图。Fig. 2 is a schematic structural diagram of a production device for extracting liquid of reconstituted tobacco leaf raw materials disclosed in an embodiment of the present invention.
其中，各部件名称如下：Among them, the names of the components are as follows:
1-原料罐；2-第一输送泵，3-超重力设备，4-压滤机，5-加热浓缩罐，6-第一冷凝器，7-第二冷凝器，8-缓冲罐，9-第二输送泵，10-产品罐。1-Raw material tank; 2-First transfer pump, 3-Ultragravity equipment, 4-Filter press, 5-Heating concentration tank, 6-First condenser, 7-Second condenser, 8-Buffer tank, 9 - Second delivery pump, 10 - Product tank.
具体实施方式Detailed ways
有鉴于此，本发明的核心在于提供一种再造烟叶原料提取液的生产方法，不仅可以解决烟梗液难于处理的问题，还能够有效提高产品的提取率。In view of this, the core of the present invention is to provide a production method of extracting liquid of reconstituted tobacco leaf raw material, which can not only solve the problem that the tobacco stem liquid is difficult to handle, but also effectively improve the extraction rate of the product.
本发明的另一核心还在于提供一种再造烟叶原料提取液的生产装置。Another core of the present invention is to provide a production device for extracting liquid of reconstituted tobacco leaf raw materials.
为了使本技术领域的人员更好地理解本发明方案，下面接合附图和具体实施方式对本发明作进一步的详细说明，请参考图1至图2。In order to enable those skilled in the art to better understand the solution of the present invention, the present invention will be further described in detail below with reference to the accompanying drawings and specific embodiments, please refer to FIG. 1 to FIG. 2 .
请参考图1，本发明实施例所公开的再造烟叶原料提取液的生产方法，包括以下步骤：Please refer to Fig. 1, the production method of the reconstituted tobacco leaf raw material extract disclosed in the embodiment of the present invention comprises the following steps:
S100：将烟叶或烟梗粉碎为烟草粉；S100: crushing tobacco leaves or tobacco stems into tobacco powder;
S200：将溶剂加入烟草粉进行搅拌，直至搅拌成烟草桨，溶剂的温度设置为第一预设温度值；S200: adding the solvent to the tobacco powder and stirring until the tobacco paddle is formed, and the temperature of the solvent is set to the first preset temperature value;
S300：将烟草桨输送至超重力设备3中，在超重力设备3中，对烟草桨中的有效物质进行提取；S300: transporting the tobacco paddle to the hypergravity device 3, and extracting the effective substance in the tobacco paddle in the hypergravity device 3;
S400：对提取后的烟草桨进行压滤，得到滤渣和滤液，滤渣用于制作再造烟叶，滤液用于再造烟叶涂布液使用。S400: Press-filter the extracted tobacco paddle to obtain a filter residue and a filtrate, the filter residue is used to make reconstituted tobacco leaves, and the filtrate is used as a coating liquid for reconstituted tobacco leaves.
当对再造烟叶原料提取液进行生产时，首先需将烟叶或烟梗粉碎为烟草粉，然后将溶剂加入烟草粉内进行搅拌，直至搅拌成烟草桨，其中溶剂的温度为预设温度值，然后再将烟草桨输送至超重力设备3中，对烟草桨中的有效物质进行提取，最后对提取后的烟草桨进行压滤，得到滤渣和滤液，其中滤渣用于制作再造烟叶，滤液用于再造烟叶涂布液使用。When producing the raw material extract of reconstituted tobacco leaves, it is first necessary to crush the tobacco leaves or tobacco stems into tobacco powder, then add the solvent into the tobacco powder and stir until it becomes a tobacco paddle, wherein the temperature of the solvent is the preset temperature value, and then The tobacco paddle is then transported to the supergravity equipment 3 to extract the effective substances in the tobacco paddle, and finally the extracted tobacco paddle is press-filtered to obtain the filter residue and filtrate, wherein the filter residue is used to make reconstituted tobacco leaves, and the filtrate is used for reconstitution Tobacco leaf coating solution is used.
和现有技术相比，采用本发明实施例所公开的再造烟叶原料提取液的生产方法，对烟草中有效物质的提取率能够超过90％，溶剂用量降低2-5倍，有效减少了能耗，提高了效益，降低了提取的时间，减少了果胶和色素的提取量，绿色环保，得到的烟草提取液可以完全适用于再造烟叶，不产生二次污染。Compared with the prior art, by adopting the production method of the raw material extract of reconstituted tobacco leaf disclosed in the embodiment of the present invention, the extraction rate of effective substances in tobacco can exceed 90%, the amount of solvent is reduced by 2-5 times, and energy consumption is effectively reduced , improve the benefit, reduce the extraction time, reduce the extraction amount of pectin and pigment, and are environmentally friendly, and the obtained tobacco extract can be completely applied to reconstituted tobacco leaves without secondary pollution.
通过试验证明，通过采用本发明实施例所公开的再造烟叶原料提取液的生产方法得到的再造烟叶原料提取液的固含量为38％-40％，波美度为24％-26％，而采用传统的方法提取后的再造烟叶原料提取液的固含量为8％，需要浓缩到固含量为38％-40％，波美度为24％-26％之间。It has been proved by experiments that the solid content of the reconstituted tobacco leaf raw material extract obtained by adopting the production method of the reconstituted tobacco leaf raw material extract disclosed in the embodiments of the present invention is 38%-40%, and the Baume degree is 24%-26%. The solid content of the raw material extract of reconstituted tobacco leaves extracted by the traditional method is 8%, which needs to be concentrated to a solid content of 38%-40% and a Baume degree of 24%-26%.
作为优选实施例，本发明实施例所公开的再造烟叶原料提取液的生产方法，在步骤S100中，烟草粉优选被粉碎至10目-200目之间。As a preferred embodiment, in the method for producing the extract liquid of the reconstituted tobacco leaf material disclosed in the embodiment of the present invention, in step S100, the tobacco powder is preferably crushed to a size between 10 mesh and 200 mesh.
作为优选实施例，本发明实施例所公开的再造烟叶原料提取液的生产方法，在步骤S200中，预设温度值优选为30℃-80℃。As a preferred embodiment, in the method for producing the raw material extract of reconstituted tobacco leaves disclosed in the embodiments of the present invention, in step S200, the preset temperature value is preferably 30°C-80°C.
作为优选实施例，本发明实施例所公开的再造烟叶原料提取液的生产方法，在步骤S200中，溶剂的重量为烟草粉的重量的2-6倍。As a preferred embodiment, in the method for producing the raw material extract of reconstituted tobacco leaf disclosed in the embodiment of the present invention, in step S200, the weight of the solvent is 2-6 times the weight of the tobacco powder.
作为优选实施例，本发明实施例所公开的再造烟叶原料提取液的生产方法，在S200中，烟草粉与溶剂在原料罐中进行搅拌，As a preferred embodiment, in the production method of the reconstituted tobacco leaf raw material extract disclosed in the embodiment of the present invention, in S200, the tobacco powder and the solvent are stirred in the raw material tank,
其中，本发明实施例所公开的原料罐上还设置有加热组件，本发明实施例对加热组件的具体结构不进行限定，只要满足本发明使用要求的结构均在本发明的保护范围之内。Wherein, the raw material tank disclosed in the embodiment of the present invention is also provided with a heating assembly. The embodiment of the present invention does not limit the specific structure of the heating assembly, as long as the structure that meets the requirements of the present invention is within the protection scope of the present invention.
作为优选实施例，本发明实施例所公开的加热组件优选采用电加热组件，当原料罐内的烟草桨需要进行加热时，可通过电加热组件对其进行加热。As a preferred embodiment, the heating assembly disclosed in the embodiment of the present invention preferably adopts an electric heating assembly, and when the tobacco paddle in the raw material tank needs to be heated, it can be heated by the electric heating assembly.
作为优选实施例，本发明实施例所公开的再造烟叶原料提取液的生产方法，在步骤S300中，烟草桨进入超重力设备3的进料速度为500kg-2000kg/h。As a preferred embodiment, in the production method of the reconstituted tobacco raw material extract disclosed in the embodiment of the present invention, in step S300, the feed rate of the tobacco paddle into the supergravity device 3 is 500kg-2000kg/h.
需要说明的是，本发明实施例所公开的再造烟叶原料提取液的生产方法，在步骤S300中，有效物质低于烟草桨中物质总量的10％。It should be noted that, in the production method of the reconstituted tobacco raw material extract disclosed in the embodiment of the present invention, in step S300, the effective substance is less than 10% of the total substance in the tobacco pulp.
需要进一步说明的是，本发明实施例所公开的再造烟叶原料提取液的生产方法，在步骤S400中，通过压滤机4对提取后的烟草桨进行压滤。It should be further explained that, in the production method of the extracted liquid of the reconstituted tobacco leaf material disclosed in the embodiment of the present invention, in step S400 , the extracted tobacco paddle is press-filtered by the filter press 4 .
作为其中一个具体实施例，本发明实施例所公开的再造烟叶原料提取液的生产方法，包括以下步骤：As one of the specific embodiments, the production method of the reconstituted tobacco leaf raw material extract disclosed in the embodiment of the present invention includes the following steps:
S100：将烟叶或烟梗600kg粉碎为烟草粉，使得烟草粉粉碎至10-200目；S100: crushing 600kg of tobacco leaves or tobacco stems into tobacco powder, so that the tobacco powder is crushed to 10-200 mesh;
S200：将烟草粉投入到原料罐中，在原料罐中加入50℃的溶剂，进行搅拌，直至搅拌成烟草桨；S200: put the tobacco powder into the raw material tank, add a solvent at 50°C into the raw material tank, and stir until it becomes a tobacco paddle;
S300：将烟草桨输送至超重力设备3中，对烟草桨中的有效物质进行提取；S300: transporting the tobacco paddle to the hypergravity device 3, and extracting effective substances in the tobacco paddle;
S400：对提取后的烟草桨进行压滤，得到滤渣和滤液，滤渣用于制作再造烟叶，滤液用于再造烟叶涂布液使用。S400:Press-filter the extracted tobacco paddle to obtain a filter residue and a filtrate, the filter residue is used to make reconstituted tobacco leaves, and the filtrate is used as a coating liquid for reconstituted tobacco leaves.
作为其中另一个具体实施例，本发明实施例所公开的再造烟叶原料提取液的生产方法，包括以下步骤：As another specific embodiment, the method for producing the extract of reconstituted tobacco raw material disclosed in the embodiment of the present invention includes the following steps:
S100：将烟叶或烟梗300kg粉碎为烟草粉，使得烟草粉粉碎至10-200目；S100: crushing 300kg of tobacco leaves or tobacco stems into tobacco powder, so that the tobacco powder is crushed to 10-200 mesh;
S200：将烟草粉投入到原料罐中，在原料罐中加入75℃的溶剂，进行搅拌，直至搅拌成烟草桨；S200: put the tobacco powder into the raw material tank, add a 75°C solvent into the raw material tank, and stir until it becomes a tobacco paddle;
S300：将烟草桨输送至超重力设备3中，对烟草桨中的有效物质进行提取；S300: transporting the tobacco paddle to the hypergravity device 3, and extracting effective substances in the tobacco paddle;
S400：对提取后的烟草桨进行压滤，得到滤渣和滤液，滤渣用于制作再造烟叶，滤液用于再造烟叶涂布液使用。S400: Press-filter the extracted tobacco paddle to obtain a filter residue and a filtrate, the filter residue is used to make reconstituted tobacco leaves, and the filtrate is used as a coating liquid for reconstituted tobacco leaves.
需要说明的是，本发明实施例所公开的溶剂优选为水。It should be noted that the solvent disclosed in the embodiments of the present invention is preferably water.
本发明实施例所公开的再造烟叶原料提取液的生产装置，应用于如上述任意一项实施例所公开的再造烟叶原料提取液的生产方法中，其中，再造烟叶原料提取液的生产装置包括原料罐1、第一输送泵2、超重力设备3、压滤机4、加热浓缩罐5、冷凝器、缓冲罐8、第二输送泵9和产品罐10。The production device of the reconstituted tobacco raw material extract disclosed in the embodiments of the present invention is applied to the production method of the reconstituted tobacco raw material extract disclosed in any one of the above embodiments, wherein the production device of the reconstituted tobacco raw material extract includes raw materials Tank 1, first delivery pump 2, supergravity equipment 3, filter press 4,
具体的，原料罐1通过第一输送泵2与超重力设备3的第一进料口相连通，超重力设备3的第一出料口与压滤机4的进料口相连通，压滤机4的出料口与加热浓缩罐5相连通，加热浓缩罐5的出料口与超重力设备3的第二进料口相连通，超重力设备3的第二出料口与冷凝器的进料口相连通，冷凝器的出料口与缓冲罐8的进料口相连通，缓冲罐8的出料口通过第二输送泵9与超重力设备3的第三进料口相连通。Specifically, the raw material tank 1 communicates with the first feed port of the supergravity equipment 3 through the first transfer pump 2, and the first discharge port of the supergravity device 3 communicates with the feed port of the filter press 4, and the press filter The discharge port of the machine 4 is connected with the
混合好后的烟草桨，从原料罐1中经过第一输送泵2将烟草桨输送至超重力设备3中，在超重力设备3中提取后进入压滤机4中，经过压滤后除去烟粉，烟粉用于再造烟叶中，得到的滤液进入加热浓缩罐5，经过浓缩得到的产品用于再造烟叶的液料中，加热浓缩产生的蒸气进入超重力设备3中，用做汽提使用，与溶剂在超重力情况下，挥发带出烟草中的挥发油，经过冷凝器冷却后进入缓冲罐8，其中将第二输送泵9的回流比调整为10:1，将9份的液体通过第二输送泵9进入产品罐10中，在产品罐10中分去水相，得到油相为烟草中的香味成分，用于再造烟叶涂布，1份的液体进入超重力设备中，达到萃取高效进行。直至萃取完成，检测渣中的有效成分低于总量的10％。The mixed tobacco paddle is transported from the raw material tank 1 to the supergravity equipment 3 through the first conveying pump 2, and after being extracted in the supergravity equipment 3, it enters the filter press 4, and the tobacco paddle is removed after pressure filtration. Powder and smoke powder are used in reconstituted tobacco leaves, and the obtained filtrate enters the heating and concentrating
和现有技术相比，采用本发明实施例所公开的再造烟叶原料提取液的生产方法，对烟草中有效物质的提取率能够超过90％，提取效率提高了，溶剂用量降低了2-5倍，减少了能耗，提高了效益，降低了提取的时间，减少了果胶和色素的提取量，绿色环保，得到的烟草提取液可以完全适用于再造烟叶，不产生二次污染。Compared with the prior art, adopting the production method of the raw material extract of reconstituted tobacco leaf disclosed in the embodiment of the present invention can extract more than 90% of effective substances in tobacco, the extraction efficiency is improved, and the amount of solvent is reduced by 2-5 times , reduces energy consumption, improves efficiency, reduces extraction time, reduces the extraction amount of pectin and pigment, is green and environmentally friendly, and the obtained tobacco extract can be completely applied to reconstituted tobacco leaves without secondary pollution.
本发明实施例所公开的再造烟叶原料提取液的生产装置中，由于通过水相萃取，环保性高，采用超重力萃取，萃取效率高，节省萃取剂，减少能量的消耗，萃取后得到水溶性的烟草有效物与油溶性的烟草提取物，对烟草有效物质进行全面的提取，得到的烟粉用于制作烟草薄片，得到的水溶性和油溶性的提取物再用于烟草薄片，与传统的提取比增加烟草薄片的抽吸性，提升了烟草薄片的烟草本味。In the production device of the reconstituted tobacco leaf raw material extract disclosed in the embodiments of the present invention, due to the water phase extraction, the environmental protection is high, and the supergravity extraction is used, the extraction efficiency is high, the extraction agent is saved, the energy consumption is reduced, and the water-soluble Tobacco effective substances and oil-soluble tobacco extracts, comprehensive extraction of tobacco effective substances, the obtained smoke powder is used to make tobacco sheets, and the obtained water-soluble and oil-soluble extracts are then used in tobacco sheets, which is different from traditional The extraction ratio increases the drawability of the tobacco sheet and enhances the tobacco flavor of the tobacco sheet.
需要说明的是，本发明实施例所公开的再造烟叶原料提取液的生产装置，冷凝器包括第一冷凝器6和第二冷凝器7，其中，第一冷凝器6的进料口与超重力设备的第二出料口相连通，第一冷凝器7的出料口与第二冷凝器7的进料口相连通，第二冷凝器7的出料口与缓冲罐8的进料口相连通。如此设置，提升对蒸气的冷凝效果。It should be noted that, in the production device of the reconstituted tobacco leaf raw material extract disclosed in the embodiment of the present invention, the condenser includes a
在本申请的描述中，需要说明的是，术语“中心”、“上”、“下”、“左”、“右”、“竖直”、“水平”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系，仅是为了便于描述本申请和简化描述，而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作，因此不能解为对本申请的限制。此外，术语“第一”、“第二”、“第三”仅用于描述目的，而不能理解为指示或暗示相对重要性。In the description of this application, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer" etc. The indicated orientation or positional relationship is based on the orientation or positional relationship shown in the drawings, and is only for the convenience of describing the present application and simplifying the description, rather than indicating or implying that the referred device or element must have a specific orientation, use a specific orientation construction and operation, and therefore should not be construed as limiting the application. In addition, the terms "first", "second", and "third" are used for descriptive purposes only, and should not be construed as indicating or implying relative importance.
除非另有明确的规定和限定，术语“安装”、“相连”、“连接”应做广义理解，例如，可以是固定连接，也可以是可拆卸连接，或一体地连接；可以是机械连接，也可以是电连接；可以是直接相连，也可以通过中间媒介间接相连，可以是两个元件内部的连通。对于本领域的普通技术人员而言，可以具体情况理解上述术语在本申请中的具体含义。Unless otherwise clearly specified and limited, the terms "installation", "connection" and "connection" should be interpreted in a broad sense, for example, it may be a fixed connection, a detachable connection, or an integral connection; it may be a mechanical connection, It can also be an electrical connection; it can be a direct connection, or an indirect connection through an intermediary, or an internal communication between two components. Those of ordinary skill in the art can understand the specific meanings of the above terms in this application in specific situations.
对所公开的实施例的上述说明，使本领域专业技术人员能够实现或使用本发明。对这些实施例的多种修改对本领域的专业技术人员来说将是显而易见的，本文中所定义的一般原理可以在不脱离本发明的精神或范围的情况下，在其它实施例中实现。因此，本发明将不会被限制于本文所示的这些实施例，而是要符合与本文所公开的原理和新颖特点相一致的最宽的范围。The above description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the invention. Therefore, the present invention will not be limited to the embodiments shown herein, but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
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