CN104722118B - Extraction device and extraction method of pure natural plant alkaloid - Google Patents
Extraction device and extraction method of pure natural plant alkaloid Download PDFInfo
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- CN104722118B CN104722118B CN201510150972.3A CN201510150972A CN104722118B CN 104722118 B CN104722118 B CN 104722118B CN 201510150972 A CN201510150972 A CN 201510150972A CN 104722118 B CN104722118 B CN 104722118B
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Abstract
The invention provides an extraction device and an extraction method of pure natural plant alkaloid. The extraction method comprises the following steps: incinerating natural organic plant straws to obtain plant ash; pulverizing and putting the plant ash to a filter; gradually filtering; fully dissolving the plant alkaloid of plant ash in each layer in a filter solution due to a special structural design of each layer; and finally obtaining a plant alkaloid solution with high concentration. In the processing process, no chemical assistants are used, and the prepared plant alkaloid is pure natural and free of toxic and side effects. The content of K2CO3 is over 6.0%. The plant alkaloid further contains trace nutrient elements such as magnesium, calcium, silicon, ferrum, manganese, copper, zinc, boron and molybdenum and is beneficial for the physical health of human body. The plant alkaloid obtained according to the scheme is wide in use, can be used for adjusting power of hydrogen in the food processing process, and is particularly suitable for being used in the beverage industry. The beverage adjusted by using the plant alkaloid is obviously better in taste than that adjusted by using chemical alkali. The byproducts can be further used as a high quality chemical fertilizer for improving the air permeability of soil in poor lands, so that both yield and income of crops are increased.
Description
Technical field
The present invention relates to a kind of extraction element of pure natural plant alkaloid and method.
Background technology
At present in food processing process, generally use soda ash as acidity regulator.The existing side manufacturing soda ash
Method has: Hou's process for soda production, natural plus mutual method, combined soda method send out despot's stone method, new rising sun method etc..First, these
The solubility salt mineral such as alkaline method sea salt, rock salt and bittern are primary raw material, by physics and
The method of chemistry is extracted crystallization and is made.There is more defect in these methods: 1, raw mineral materials exists and human body is had
The impurity of evil, in subtractive process, adds such as the auxiliary agent such as ammonia, carbon monoxide, hydrogen sulfide, leads in finished product
There is certain residual quantity in soda ash, harm is produced to health；2nd, alkaline complex manufacturing, investment big,
High cost；3rd, in industrialized production, energy consumption is big for soda ash, produces a large amount of harmful exhausts, waste water, to environment
Cause to pollute in various degree.
Content of the invention
In order to solve the above problems, the present invention proposes a kind of extraction element of pure natural plant alkaloid and method,
Carry out pre-processing using waste crop straws, process extraction and be obtained, but extraction process is simple, low cost,
Energy consumption is little, pollution is little, and the acid-base value that can serve as in food processing is adjusted.
The present invention to realize particular by technical scheme below:
A kind of extraction element of pure natural plant alkaloid, at least includes the filter tank of two same specifications, described filter tank bottom
Portion is provided with the first filter mesh layer and the second filter mesh layer, forms filtrate between described first filter mesh layer and the second filter mesh layer
Surge chamber；It is provided with liquid storage tank, described liquid storage tank is provided with finer mesh, finer mesh will store up below described filter tank
Liquid pool is divided into upper and lower two parts, and the bottom of described liquid storage tank is arranged with liquid outlet；It is provided with above described filter tank
Spray equipment, described spray equipment connects water inlet pipe；Described water inlet pipe is communicated to liquid storage tank by circulating line
Lower part, described circulating line be provided with water circulating pump and circulation gate valve.
Further, described filtrate surge chamber is provided with reflux line, and described reflux line is communicated to circulation pipe
Road, described reflux line is provided with backflow water pump and backflow gate valve.
Further, the sieve aperture quantity on described first filter mesh layer is more than the sieve aperture quantity on the second filter mesh layer.
Further, the screen number on the first filter mesh layer and the second filter mesh layer on every metafiltration pond from top to bottom
Amount gradually tails off.
A kind of extracting method of pure natural plant alkaloid is it is characterised in that comprise the following steps:
(1) natural organic plant crop straw burning is obtained plant ash, plant ash is pulverized and puts in filter tank
At least keep plant ash thickness in 50cm；
(2) spray equipment the plant ash stirring in filter tank are opened, water velocity ensures liquid in orlop filter tank
Face is in 4～6cm；
(3) measure the filtrate concentration containing alkali salt in every metafiltration pond, during less than requirements concentration, open corresponding filter
Backflow water pump and backflow gate valve that pond connects, gained filtrate is sprayed again from spray equipment；
(4) the filtrate alkali salt concentration in measurement liquid storage tank, during more than or equal to requirements concentration, opens out liquid
Mouth carries out liquid collection；During less than requirements concentration, open water circulating pump and filtrate is filled by circulation gate valve again
Dress first floor filter tank carries out filtration treatment, if the filter liquor concentration obtaining in liquid storage tank still is below requirements, changes
Plant ash；
(5) filtrate obtaining liquid outlet is sterilized, filling.
What the present invention produced has the beneficial effect that 1, production technology is relatively simple, consume energy low, low cost；2nd, add
Do not use any chemical assistant during work, the vegetable soda produced is natural, no toxicity, side effect, also contain magnesium,
The micronutrient elements such as calcium, zinc, manganese, beneficial person health；3rd, no poisonous and harmful pollution in process
Thing produces, and environmental pollution is little.4th, byproduct fertilizer can help peasant's increasing both production and income；5th, make full use of
Crop waste stalk, it is to avoid the environmental pollution that extensive burning brings.
Brief description
In order to be illustrated more clearly that the embodiment of the present invention or technical scheme of the prior art, below will be to enforcement
Example or description of the prior art in required use accompanying drawing be briefly described it should be apparent that, below describe
In accompanying drawing be only some embodiments of the present invention, for those of ordinary skill in the art, do not paying
On the premise of going out creative work, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is the extraction element structural representation of the present invention.
Specific embodiment
Below in conjunction with the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clearly and completely
Description is it is clear that described embodiment is only a part of embodiment of the present invention, rather than whole enforcement
Example.Based on the embodiment in the present invention, those of ordinary skill in the art are not making creative work premise
Lower obtained every other embodiment, broadly falls into the scope of protection of the invention.
As shown in figure 1, a kind of extraction element of pure natural plant alkaloid, at least include the filter tank 3 of two same specifications,
Described filter tank 3 bottom is provided with the first filter mesh layer 4 and the second filter mesh layer 5, described first filter mesh layer 4 and the second filter
Form filtrate surge chamber 15 between stratum reticulare 5；It is provided with liquid storage tank 10, described liquid storage tank 10 below described filter tank 3
It is provided with finer mesh 13, liquid storage tank is divided into upper and lower two parts by finer mesh 13, described liquid storage tank 10
Bottom is arranged with liquid outlet 14；It is provided with spray equipment 2, described spray equipment 2 connects above described filter tank 3
Water inlet pipe 1；Described water inlet pipe 1 is communicated to the lower part of liquid storage tank 10, described circulation by circulating line 8
Pipeline 8 is provided with water circulating pump 11 and circulation gate valve 12.
Further in order to avoid the plant ash filtrate salt content that causes too long of spray is too low, filtrate surge chamber 15
It is provided with reflux line 9, described reflux line 9 is communicated to circulating line 8, described reflux line 9 is provided with
Backflow water pump 6 and backflow gate valve 7.In order to ensure that every layer of plant ash can be substantially immersed in solution, obtain simultaneously
The filter liquor concentration obtaining reaches maximization, and the sieve aperture quantity on the first filter mesh layer is more than the sieve aperture on the second filter mesh layer
Quantity, when arranging multilayer filter tank, the first filter mesh layer on every metafiltration pond from top to bottom and the second filter mesh layer
On sieve aperture quantity gradually tail off.The filtrate so being fallen by the superiors can step by step every layer dissolving plant ash in
DDGS, in orlop ensure solution concentration maximize.
A kind of extracting method of pure natural plant alkaloid, comprises the following steps:
(1) natural organic plant crop straw burning is obtained plant ash, plant ash is pulverized and puts in filter tank
At least keep plant ash thickness in 50cm；
(2) spray equipment the plant ash stirring in filter tank are opened, water velocity ensures liquid in orlop filter tank
Face is in 4～6cm；
(3) measure the filtrate concentration containing alkali salt in every metafiltration pond, during less than requirements concentration, open corresponding filter
Backflow water pump and backflow gate valve that pond connects, gained filtrate is sprayed again from spray equipment；
(4) the filtrate alkali salt concentration in measurement liquid storage tank, during more than or equal to requirements concentration, opens out liquid
Mouth carries out liquid collection；During less than requirements concentration, open water circulating pump and filtrate is filled by circulation gate valve again
Dress first floor filter tank carries out filtration treatment, if the filter liquor concentration obtaining in liquid storage tank still is below requirements, changes
Plant ash；
(5) filtrate obtaining liquid outlet is sterilized, filling.
This method chooses organic rice straw, reduces heavy metal, the residual quantity of agricultural chemicals of raw material, from source
Upper control food security, controls and filters link in vegetable soda process, it is to avoid contain bulky grain in product different
Thing it is ensured that food additives safe and reliable, do not use any chemical assistant in process, produce
Vegetable soda is natural, k2co3Content more than 6.0%, no toxicity, side effect, also contain magnesium, calcium, zinc, manganese etc.
Micronutrient element, beneficial person health.The vegetable soda that the present invention obtains is of many uses, and it can be used for eating
In product process, acid-base value is adjusted, and is particluarly suitable for beverage industry and uses, with its beverage mouthfeel after adjusting
Significantly better than chemical bases, its byproduct also can make high-quality chemical fertilizer, improve the aeration of barren field soil, make
Increasing crop yield increases income.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all at this
Within bright spirit and principle, any modification, equivalent substitution and improvement made etc., should be included in this
Within bright protection domain.
Claims (2)
1. a kind of extraction element of pure natural plant alkaloid is it is characterised in that at least include the filter of two same specifications
Pond, described filter tank bottom is provided with the first filter mesh layer and the second filter mesh layer, described first filter mesh layer and the second filter screen
Form filtrate surge chamber between layer；It is provided with liquid storage tank, described liquid storage tank is provided with finer mesh below described filter tank,
Liquid storage tank is divided into upper and lower two parts by finer mesh, and the bottom of described liquid storage tank is arranged with liquid outlet；Described
It is provided with spray equipment, described spray equipment connects water inlet pipe above filter tank；Described water inlet pipe passes through circulating line
It is communicated to the lower part of liquid storage tank, described circulating line is provided with water circulating pump and circulation gate valve；Described first filter
Sieve aperture quantity on stratum reticulare is more than the sieve aperture quantity on the second filter mesh layer, the on every metafiltration pond from top to bottom
Sieve aperture quantity on one filter mesh layer and the second filter mesh layer gradually tails off.
2. as claimed in claim 1 a kind of extraction element of pure natural plant alkaloid it is characterised in that described
Filtrate surge chamber is provided with reflux line, and described reflux line is communicated to circulating line, on described reflux line
It is provided with backflow water pump and backflow gate valve.
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| CN201510150972.3A CN104722118B (en) | 2015-04-01 | 2015-04-01 | Extraction device and extraction method of pure natural plant alkaloid |
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| CN201510150972.3A CN104722118B (en) | 2015-04-01 | 2015-04-01 | Extraction device and extraction method of pure natural plant alkaloid |
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| CN104722118B true CN104722118B (en) | 2017-01-18 |
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| CN105439864A (en) * | 2015-12-31 | 2016-03-30 | 常州市长宇实用气体有限公司 | Method for extracting high-purity ferulic acid from Szechwan lovage rhizome stems |
| CN106422500A (en) * | 2016-08-08 | 2017-02-22 | 张开基 | Production apparatus and production method of all-natural highly-pure solid edible plant ash alkali |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101172888A (en) * | 2007-10-23 | 2008-05-07 | 徐秀山 | Stalk ash slag leaching method |
| CN101983950B (en) * | 2010-05-21 | 2012-11-21 | 淮安市农业科学研究院 | Method for extracting potassium salt from plant ash by eluting and filtering in grades |
| CN201704221U (en) * | 2010-05-28 | 2011-01-12 | 淮安市农业科学研究院 | Device for extracting potassium salts in plant ashes by double-tank superposition method |
| CN202829859U (en) * | 2012-08-08 | 2013-03-27 | 江苏徐淮地区淮阴农业科学研究所 | Multi-tank device used for extracting plant ash sylvine and provided with turnover method |
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Effective date of registration: 20180831 Address after: 430040 the 209, 210, 211, 218, 219 rooms of No. 6, Zan Ma Ling renovation Road, Dongxihu District, Wuhan, Hubei Patentee after: Wuhan Baicu grass and Wood Technology Co., Ltd. Address before: 430040 between the 107 National Road southwest, the dongma ridge eleven ditch and the twelve ditch in Wuhan, Hubei. Patentee before: Qin Yuan Beverage Company Limited of Wuhan City |