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CN115646656A - A kind of activation method and application of optimizing mechanically activated starch inhibitor - Google Patents

A kind of activation method and application of optimizing mechanically activated starch inhibitor Download PDF

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CN115646656A
CN115646656A CN202211225872.9A CN202211225872A CN115646656A CN 115646656 A CN115646656 A CN 115646656A CN 202211225872 A CN202211225872 A CN 202211225872A CN 115646656 A CN115646656 A CN 115646656A
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starch
flotation
mechanically activated
inhibitor
recovery rate
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CN115646656B (en
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杨思原
王宣
张浩峰
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Wuhan University of Technology WUT
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Abstract

本发明公开一种优化机械活化淀粉抑制剂的活化方法及应用,包括以下步骤:S1.以淀粉为原料,通过调整机械活化参数集合,以对淀粉原料进行充能,得到不同参数条件下的机械活化淀粉抑制剂,并通过充能能量公式(Ⅰ)计算各机械活化淀粉抑制剂的充能能量值,

Figure DDA0003879671420000011
S2.以机械活化淀粉为抑制剂,分别对矿物进行浮选实验,并记录浮选回收率;S3.通过SPSS拟合对应的充能能量值及浮选回收率,得到回收率‑充能公式(Ⅱ),ε=αE2+βE+γ(Ⅱ);S4.通过回收率‑充能公式(Ⅱ)计算充能能量值Ei,将Ei带入充能能量公式(Ⅰ)中确定机械活化参数集合,采用所确定的参数制备的淀粉抑制剂反应活性强、抑制矿物浮选效率高。

Figure 202211225872

The invention discloses an activation method and application for optimizing mechanically activated starch inhibitors, including the following steps: S1. Using starch as a raw material, by adjusting the set of mechanical activation parameters, the starch raw material is charged to obtain mechanical activation under different parameter conditions. Activate the starch inhibitor, and calculate the charging energy value of each mechanically activated starch inhibitor by the charging energy formula (I),

Figure DDA0003879671420000011
S2. Using mechanically activated starch as an inhibitor, carry out flotation experiments on minerals respectively, and record the flotation recovery rate; S3. Fit the corresponding charging energy value and flotation recovery rate through SPSS to obtain the recovery rate-charging formula (II), ε=αE 2 +βE+γ(II); S4. Calculate the charging energy value E i through the recovery rate-charging formula (II), and bring E i into the charging energy formula (Ⅰ) to determine A set of mechanical activation parameters, the starch inhibitor prepared by using the determined parameters has strong reactivity and high inhibitory mineral flotation efficiency.

Figure 202211225872

Description

一种优化机械活化淀粉抑制剂的活化方法及应用A kind of activation method and application of optimizing mechanically activated starch inhibitor

技术领域technical field

本发明涉及矿物加工技术领域,尤其涉及一种优化机械活化淀粉抑制剂的活化方法及应用。The invention relates to the technical field of mineral processing, in particular to an activation method and application for optimizing a mechanically activated starch inhibitor.

背景技术Background technique

天然淀粉品种有限,且存在冷水不溶、糊的热稳定性差、抗剪切性能低,冷后易脱水、易老化、成膜性差以及缺乏耐水能力等缺点,同时在现代工业中广泛采用新工艺、新设备、新技术等情况下的应用范围有限,已不能满足日益发展的现代工艺和设备的需要,因此,需要对淀粉进行变性处理。There are limited varieties of natural starch, and there are disadvantages such as insolubility in cold water, poor thermal stability of paste, low shear resistance, easy dehydration after cold, easy aging, poor film formation and lack of water resistance. At the same time, new processes, The scope of application of new equipment and new technologies is limited, and it can no longer meet the needs of the growing modern technology and equipment. Therefore, starch needs to be denatured.

淀粉变性就是采用物理、化学或生物学的手段改变天然淀粉的性质,通过分子切断、重排、氧化或在淀粉分子中引入取代基可制得性质发生变化的淀粉衍生物,即变性淀粉,用以增加其性能或引进新特性,克服应用时的缺陷,以适应现代工业生产的需要;物理手段包括机械活化,是指物品在机械力作用下会产生晶格畸变和局部破坏,并形成各种缺陷,导致其内能增大,反应活性增强的过程。Starch denaturation is the use of physical, chemical or biological means to change the properties of native starch, through molecular cutting, rearrangement, oxidation or the introduction of substituents in starch molecules to obtain starch derivatives with changed properties, that is, modified starch. To increase its performance or introduce new features, overcome the defects in application, and meet the needs of modern industrial production; physical means include mechanical activation, which means that the item will produce lattice distortion and local destruction under the action of mechanical force, and form various Defects lead to the increase of its internal energy and the process of enhanced reactivity.

淀粉作为天然大分子化合物,常以抑制剂在矿物浮选中应用,即选择性抑制某些矿物浮选,扩大不同矿物间的可浮性差异,得以提高浮选分选效率。然而,现有研究暂未明确机械活化方式对淀粉分子抑制矿物浮选能力的影响,也未有机械活化改性淀粉在矿物浮选领域的应用。因此,有必要探索机械活化条件对淀粉分子抑制能力的影响,并明确制备淀粉抑制剂的最佳工艺条件,使其在矿物浮选应用中的分选效率得以提高。As a natural macromolecular compound, starch is often used as an inhibitor in mineral flotation, that is, to selectively inhibit the flotation of certain minerals, expand the difference in floatability between different minerals, and improve the efficiency of flotation and separation. However, the existing research has not yet clarified the effect of mechanical activation on the ability of starch molecules to inhibit mineral flotation, and there is no application of mechanically activated modified starch in the field of mineral flotation. Therefore, it is necessary to explore the effect of mechanical activation conditions on the inhibitory ability of starch molecules, and to clarify the optimal process conditions for the preparation of starch inhibitors, so that their separation efficiency in mineral flotation applications can be improved.

发明内容Contents of the invention

有鉴于此,本申请提供一种优化机械活化淀粉抑制剂的活化方法及应用,通过所确定的参数制备的淀粉抑制剂活性高,矿物分选效率高。In view of this, the present application provides an activation method and application of an optimized mechanically activated starch inhibitor. The starch inhibitor prepared by the determined parameters has high activity and high mineral separation efficiency.

为达到上述技术目的,本申请采用以下技术方案:In order to achieve the above-mentioned technical purpose, the application adopts the following technical solutions:

第一方面,本申请提供一种优化机械活化淀粉抑制剂的活化方法,包括以下步骤:In a first aspect, the application provides a method for optimizing the activation of mechanically activated starch inhibitors, comprising the following steps:

S1.以淀粉为原料,调整行星磨的机械活化参数集合,进行干法机械活化固相反应,以对淀粉原料进行充能,得到不同参数条件下的机械活化淀粉抑制剂,计算各机械活化淀粉抑制剂的充能能量值;S1. Using starch as a raw material, adjust the mechanical activation parameter set of the planetary mill, and perform a dry mechanical activation solid-phase reaction to charge the starch raw material, obtain mechanically activated starch inhibitors under different parameter conditions, and calculate each mechanically activated starch Inhibitor charge energy value;

S2.以机械活化淀粉为抑制剂,分别对矿物进行浮选实验,并记录浮选回收率;S2. Using mechanically activated starch as an inhibitor, carry out flotation experiments on minerals respectively, and record the flotation recovery rate;

S3.通过SPSS拟合对应的充能能量值及浮选回收率,得到回收率-充能公式(Ⅱ),S3. Fit the corresponding charging energy value and flotation recovery rate through SPSS to obtain the recovery rate-charging formula (II),

ε=αE2+βE+γ(Ⅱ),ε=αE 2 +βE+γ(II),

其中ε为浮选回收率;α、β、γ为由淀粉种类确定的常数;Among them, ε is the flotation recovery rate; α, β, γ are constants determined by the type of starch;

S4.通过回收率-充能公式(Ⅱ)计算最佳充能能量值Ei,将Ei带入充能能量公式(Ⅰ)中反推确定最佳机械活化参数集合;S4. Calculate the optimal charging energy value E i through the recovery rate-charging formula (II), and bring E i into the charging energy formula (I) to determine the optimal mechanical activation parameter set;

S5.基于最佳机械活化参数集合,制备机械活化淀粉抑制剂。S5. Based on the optimal set of mechanical activation parameters, prepare a mechanically activated starch inhibitor.

优选的,步骤S4中,最佳充能能量值Ei的计算方法为,将回收率-充能公式(Ⅱ)求导等于零,求解取极值即为最佳充能能量值EiPreferably, in step S4, the optimal charging energy value E i is calculated by deriving the recovery rate-charging formula (II) to be equal to zero, and obtaining the extreme value is the optimal charging energy value E i .

优选的,淀粉原料包括玉米淀粉、马铃薯淀粉、糯米淀粉、大米淀粉等中的一种或几种。Preferably, the starch raw material includes one or more of corn starch, potato starch, glutinous rice starch, rice starch and the like.

优选的,步骤S4中,机械活化参数集合包括球料比、行星磨转速、活化时间三项参数;将最佳充能能量值Ei带入充能能量公式(Ⅰ)中,基于机械活化参数集合中的任意两项参数计算得到剩余一项参数,并将所获得的三项参数记为最佳机械活化参数集合。Preferably, in step S4, the mechanical activation parameter set includes three parameters: ball-to-material ratio, planetary mill speed, and activation time; the optimal charge energy value E i is brought into the charge energy formula (I), based on the mechanical activation parameters Any two parameters in the set are calculated to obtain the remaining one parameter, and the obtained three parameters are recorded as the optimal mechanical activation parameter set.

优选的,步骤S1中,充能能量值的范围为2.6KJ-32KJ。Preferably, in step S1, the charging energy value ranges from 2.6KJ to 32KJ.

优选的,浮选实验的步骤为,在待浮选的矿样中加入去离子水,并调整pH至碱性,加入机械活化淀粉抑制剂的水溶液,搅拌后,再加入捕收剂,搅拌、浮选刮泡,过滤槽内产物,烘干、称重,得浮选精矿的品位和回收率。Preferably, the steps of the flotation experiment are: add deionized water to the ore sample to be flotation, and adjust the pH to alkaline, add the aqueous solution of mechanically activated starch inhibitor, after stirring, add the collector, stir, Flotation scraping, filtering the product in the tank, drying and weighing to obtain the grade and recovery rate of the flotation concentrate.

优选的,充能能量值由充能能量公式(Ⅰ)计算得到,Preferably, the charging energy value is calculated by the charging energy formula (I),

Figure BDA0003879671400000031
Figure BDA0003879671400000031

其中,E为充能能量、f为淀粉活化指数、τ为球料比、ei为行星磨的单位能耗、N为行星磨转速、T为活化时间。Among them, E is the charging energy, f is the starch activation index, τ is the pellet ratio, e i is the unit energy consumption of the planetary mill, N is the rotational speed of the planetary mill, and T is the activation time.

第二方面,本申请提供一种机械活化淀粉抑制剂。In a second aspect, the present application provides a mechanically activated starch inhibitor.

第三方面,本申请提供一种机械活化淀粉抑制剂在矿物分选中的应用。In a third aspect, the present application provides an application of a mechanically activated starch inhibitor in mineral sorting.

优选的,矿物包括赤铁矿、重晶石、高岭石等中的一种或几种。Preferably, the minerals include one or more of hematite, barite, kaolinite and the like.

本申请的有益效果如下:The beneficial effects of the application are as follows:

本发明中充能能量公式和回收率-充能公式能控制淀粉抑制剂品质,得到抑制效果最佳的机械活化淀粉成品,并且可以确定机械活化淀粉最佳输入能量以及最佳机械活化条件的组合,优化淀粉抑制剂制备工艺;In the present invention, the charging energy formula and the recovery rate-charging formula can control the quality of the starch inhibitor, obtain the mechanically activated starch product with the best inhibitory effect, and can determine the combination of the optimal input energy of the mechanically activated starch and the optimal mechanical activation conditions , optimize the preparation process of starch inhibitor;

通过本发明的方法调节行星磨时间、转数以及球料比,精准控制得到的淀粉抑制剂,在不破坏淀粉内部结构下,使淀粉获得活化特性,增加其溶解度,同时降低了淀粉的糊化温度及凝沉性;Through the method of the present invention, the starch inhibitor obtained can be precisely controlled by adjusting the planetary milling time, the number of revolutions, and the ball-to-material ratio. Without destroying the internal structure of the starch, the starch can obtain activation characteristics, increase its solubility, and reduce the gelatinization of the starch. temperature and settling;

将所得到的淀粉抑制剂用于矿物浮选,由于机械活化淀粉的反应活性高,有效提高了其在浮选时与部分矿物表面的作用能力,使该矿物亲水并阻碍了捕收剂的结合,从而选择性降低部分矿物的浮选回收率,得以提高分选效率。The obtained starch inhibitor is used in mineral flotation. Due to the high reactivity of mechanically activated starch, it effectively improves its ability to interact with the surface of some minerals during flotation, making the mineral hydrophilic and hindering the collection of collectors. Combined, thereby selectively reducing the flotation recovery rate of some minerals, and improving the separation efficiency.

附图说明Description of drawings

图1为不同机械活化时间条件下制备的玉米淀粉抑制剂对赤铁矿的浮选回收率的作用结果比较图;Fig. 1 is the effect comparison figure of the cornstarch inhibitor prepared under the condition of different mechanical activation time to the flotation recovery rate of hematite;

图2为不同行星式球磨机转速条件下玉米淀粉抑制剂对赤铁矿的浮选回收率的作用结果比较图;Fig. 2 is the effect comparison figure of the effect of corn starch inhibitor on the flotation recovery rate of hematite under different planetary ball mill rotating speed conditions;

图3为不同球料比条件下制备的玉米淀粉抑制剂对赤铁矿的浮选回收率的作用结果比较图;Fig. 3 is the comparative figure of the action result of the flotation recovery rate of the cornstarch inhibitor prepared under different pellet ratio conditions to hematite;

图4为玉米淀粉抑制剂回收率-充能公式函数关系式图;Fig. 4 is the rate of recovery of cornstarch inhibitor-charging formula function relation figure;

图5为本方案的技术路线图。Figure 5 is the technical roadmap of this solution.

具体实施方式Detailed ways

为了使本发明的目的、技术方案及优点更加清楚明白,以下结合实施例,对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅仅用以解释本发明,并不用于限定本发明。In order to make the object, technical solution and advantages of the present invention more clear, the present invention will be further described in detail below in conjunction with the examples. It should be understood that the specific embodiments described here are only used to explain the present invention, not to limit the present invention.

术语解释Terminology Explanation

“淀粉活化指数”是指不同淀粉对于机械活化充能的转化效率,由各淀粉本身的属性决定;"Starch activation index" refers to the conversion efficiency of different starches for mechanical activation and charging, which is determined by the properties of each starch itself;

“行星磨的单位能耗”是指通过所选择的行星磨仪器的额定功率;"The unit energy consumption of the planetary mill" refers to the rated power of the selected planetary mill instrument;

“充能能量”是指淀粉原料经行星磨的机械活动能量转换获得的输入能量。"Energizing energy" refers to the input energy obtained by converting the starch raw material through the mechanical activity energy conversion of the planetary mill.

如本领域技术人员所公知,机械活化手段是指物品在机械力作用下会产生晶格畸变和局部破坏,并形成各种缺陷,导致其内能增大,反应活性增强的过程。随着机械活化设备的不断更行迭代,对于物品输入能量的控制越来越精确,越来越容易计算,并便于模拟拟合。因此机械活化设备能够控制物品成品品质,这为得到效果最佳的活化产物,并能确定该物品最佳输入能量提供了思路。As known to those skilled in the art, mechanical activation refers to a process in which an item undergoes lattice distortion and local destruction under the action of mechanical force, and forms various defects, resulting in an increase in its internal energy and enhanced reactivity. With the continuous update and iteration of mechanical activation equipment, the control of the input energy of the item is becoming more and more accurate, easier to calculate, and easier to simulate and fit. Therefore, mechanical activation equipment can control the quality of the finished product, which provides an idea for obtaining the best activated product and determining the best input energy for the item.

本申请人发现,机械活化能强化淀粉羟基官能团活性并改变优化淀粉分子与矿物表面的作用结构,而过多的能量输入则会削弱淀粉分子的链状结构从而极大降低其抑制能力,而通过数据拟合得到公式,可反推得到最佳活化参数,控制淀粉抑制剂品质,得到抑制效果最佳的机械活化淀粉成品,并且可以确定机械活化淀粉最佳输入能量以及最佳机械活化条件,优化淀粉抑制剂制备工艺。The applicant found that mechanical activation can strengthen the activity of starch hydroxyl functional groups and change and optimize the interaction structure between starch molecules and mineral surfaces, while excessive energy input will weaken the chain structure of starch molecules and greatly reduce its inhibitory ability. The formula obtained by data fitting can be reversed to obtain the optimal activation parameters, control the quality of the starch inhibitor, and obtain the mechanically activated starch product with the best inhibition effect, and can determine the optimal input energy and the best mechanical activation conditions for mechanically activated starch, optimize Preparation process of starch inhibitor.

基于以上,创立了本发明。Based on the above, the present invention has been established.

本申请提供一种优化机械活化淀粉抑制剂的活化方法,如图5所示,包括以下步骤:The application provides a method for optimizing the activation of mechanically activated starch inhibitors, as shown in Figure 5, comprising the following steps:

S1.以淀粉为原料,称量后放至于行星磨氧化锆罐内备用,设定行星磨参数,进行机械活化:调节行星磨转数、时间以及球料比,对淀粉进行机械活化充能,制备得到不同的淀粉抑制剂备用;上述机械活化过程即干法球磨的过程,可使淀粉原料得以充能,按照不同的行星磨参数,根据充能能量公式(Ⅰ)计算对应的充能能量值E1、E2、E3、E4、E5、E6…,S1. Use starch as raw material, weigh it and put it in the zirconia tank of the planetary mill for standby, set the parameters of the planetary mill, and perform mechanical activation: adjust the rotation number, time and ball-to-material ratio of the planetary mill to mechanically activate and charge the starch. Prepare different starch inhibitors for use; the above mechanical activation process is the process of dry ball milling, which can charge the starch raw material, and calculate the corresponding charging energy value according to the charging energy formula (I) according to different planetary milling parameters E 1 , E 2 , E 3 , E 4 , E 5 , E 6 ...,

Figure BDA0003879671400000051
Figure BDA0003879671400000051

其中,E为充能能量、f为淀粉活化指数、τ为球料比、ei为行星磨的单位能耗、N为行星磨转速、T为活化时间;Among them, E is the charging energy, f is the starch activation index, τ is the pellet ratio, e i is the unit energy consumption of the planetary mill, N is the rotational speed of the planetary mill, and T is the activation time;

S2.以得到的淀粉抑制剂为溶质,去离子水为溶剂,配置成0.8g/L淀粉抑制剂溶液;以上述淀粉抑制剂溶液为抑制剂对不同的矿物进行浮选分离,包括以下步骤(赤铁矿浮选为例):将2g赤铁矿(200~400目)加入浮选槽,加入25ml去离子水搅拌2min,形成矿浆,将矿浆的pH调整至10,搅拌2min,加入机械活化淀粉抑制剂的水溶液(2ml),使浮选槽内淀粉抑制剂浓度为40mg/L,搅拌2min后,再加入1mL 1.6g/L十二胺捕收剂,搅拌2min,再加入2滴起泡剂,经浮选刮泡,将槽内矿物过滤、烘干、称重,记录称重数据,回收率为槽内精矿质量与所称取的待浮选矿样的质量比,计算得出对应的选矿回收率ε1、ε2、ε3、ε4、ε5、ε6…;S2. take the obtained starch inhibitor as solute, and deionized water as solvent, configure 0.8g/L starch inhibitor solution; use above-mentioned starch inhibitor solution as inhibitor to carry out flotation separation to different minerals, comprising the following steps ( Hematite flotation as an example): put 2g hematite (200-400 mesh) into the flotation cell, add 25ml deionized water and stir for 2 minutes to form a slurry, adjust the pH of the slurry to 10, stir for 2 minutes, add mechanical activation Aqueous solution of starch inhibitor (2ml), so that the concentration of starch inhibitor in the flotation tank is 40mg/L, after stirring for 2min, add 1mL of 1.6g/L dodecylamine collector, stir for 2min, then add 2 drops of foaming After flotation and scraping, the minerals in the tank are filtered, dried, weighed, and the weighing data is recorded. The recovery rate is the mass ratio of the concentrate quality in the tank to the mass ratio of the ore sample to be weighed to be flotation. Corresponding dressing recovery ε 1 , ε 2 , ε 3 , ε 4 , ε 5 , ε 6 ...;

S3.收集步骤S1中不同参数条件下得到的充能能量值E1、E2、E3、E4、E5、E6…,收集对应充能能量的淀粉抑制剂的选矿回收率ε1、ε2、ε3、ε4、ε5、ε6…,将上述数据进行SPSS拟合,得到充能能量值及浮选回收率的关系式,即回收率-充能公式(Ⅱ),S3. Collect the charging energy values E 1 , E 2 , E 3 , E 4 , E 5 , E 6 ... obtained under different parameter conditions in step S1, and collect the beneficiation recovery rate ε 1 of the starch inhibitor corresponding to the charging energy . _ _ _ _

ε=αE2+βE+γ(Ⅱ),ε=αE 2 +βE+γ(II),

其中ε为浮选回收率;α、β、γ为回收率-充能公式常数,随淀粉的变化而变化;Among them, ε is the flotation recovery rate; α, β, γ are the constants of the recovery rate-charging formula, which change with the change of starch;

S4.通过回收率-充能公式(Ⅱ)计算最佳充能能量值Ei,最佳充能能量值Ei的计算方法为,将回收率-充能公式(Ⅱ)求导等于零,求解取极值即为最佳充能能量值Ei,将Ei带入充能能量公式(Ⅰ)中反推确定最佳机械活化参数集合,反推过程中将三个参数中的2个设为范围内的定量以确定剩余参数的值:基于机械活化参数集合中的任意两项参数计算得到剩余一项参数,并将所获得的三项参数记为最佳机械活化参数集合。S4. Calculate the optimal charging energy value E i through the recovery rate-charging formula (II), the calculation method of the optimal charging energy value E i is to derivate the recovery rate-charging formula (II) equal to zero, and solve The extreme value is taken as the optimal charging energy value E i , and E i is brought into the charging energy formula (Ⅰ) to deduce the optimal mechanical activation parameter set. During the deduction process, two of the three parameters are set to For quantification within the range to determine the value of the remaining parameters: calculate the remaining one parameter based on any two parameters in the mechanical activation parameter set, and record the obtained three parameters as the best mechanical activation parameter set.

S5.基于最佳机械活化参数集合,制备机械活化淀粉抑制剂。S5. Based on the optimal set of mechanical activation parameters, prepare a mechanically activated starch inhibitor.

为验证理论与实际应用是否匹配,将本方案对应得到的适宜机械活化条件,制备淀粉抑制剂,并按照步骤S2中的相同条件进行浮选实验,检验浮选回收率,验证回收率-充能公式准确性,得到本方案中,能量充能公式和回收率-充能公式拟合优度均大于0.9。In order to verify whether the theory matches the actual application, the appropriate mechanical activation conditions corresponding to this scheme were prepared to prepare the starch inhibitor, and the flotation experiment was carried out according to the same conditions in step S2 to check the flotation recovery rate and verify the recovery rate-charging According to the accuracy of the formula, in this scheme, the goodness of fit of the energy charging formula and the recovery rate-charging formula is greater than 0.9.

本方案的充能能量公式(Ⅰ)与回收率-充能公式(Ⅱ)为淀粉抑制剂的制备参数选定提供理论支持,在淀粉抑制剂制备过程中起着至关重要的作用:一是提高淀粉抑制剂品质,得到抑制效果最佳的机械活化淀粉成品;二是确定机械活化淀粉最佳输入能量,对应选择最优机械活化条件,优化淀粉抑制剂制备工艺。机械活化淀粉可以抑制剂形式,应用于多种矿物的浮选之中,有效的分离目的矿物与脉石矿物。The charging energy formula (I) and recovery rate-charging formula (II) of this scheme provide theoretical support for the selection of the preparation parameters of the starch inhibitor, and play a vital role in the preparation process of the starch inhibitor: First, Improve the quality of starch inhibitors to obtain mechanically activated starch products with the best inhibitory effect; the second is to determine the optimal input energy for mechanically activated starch, correspondingly select the optimal mechanical activation conditions, and optimize the preparation process of starch inhibitors. Mechanically activated starch can be used as an inhibitor in the flotation of various minerals to effectively separate target minerals and gangue minerals.

淀粉原料包括玉米淀粉、马铃薯淀粉、糯米淀粉、大米淀粉等中的一种或几种,不同的淀粉原料对应得到不同的淀粉抑制剂,例如通过上述步骤S1,玉米淀粉(NS)原料经干法机械活化固相反应得到机械活化玉米淀粉(NST)、糯米淀粉(WS)淀粉原料经干法机械活化固相反应得到机械活化糯米淀粉(WST)、G50转基因玉米淀粉经干法机械活化固相反应得到机械活化G50转基因玉米淀粉(G50T)、G80转基因玉米淀粉经干法机械活化固相反应得到机械活化G80转基因玉米淀粉(G80T)。Starch raw materials include one or more of corn starch, potato starch, glutinous rice starch, rice starch, etc. Different starch raw materials correspond to different starch inhibitors. For example, through the above step S1, corn starch (NS) raw materials are dry-processed Mechanically activated solid phase reaction to obtain mechanically activated corn starch (NST) and waxy rice starch (WS) Starch raw materials were mechanically activated by dry solid state reaction to obtain mechanically activated glutinous rice starch (WST), and G50 transgenic corn starch was obtained by dry mechanically activated solid phase reaction The mechanically activated G50 transgenic cornstarch (G50T) was obtained, and the G80 transgenic cornstarch was mechanically activated and solid-phase reacted to obtain the mechanically activated G80 transgenic cornstarch (G80T).

值得说明的是,充能能量公式(Ⅰ)中,f为淀粉活化常数,是指不同淀粉对于机械活化充能的转化效率,由各淀粉本身的属性决定,如普通玉米的淀粉常数f为1.26;ei为行星磨的单位能耗,通过所选择的行星磨仪器的功率换算得到,本申请中,所使用的行星磨为德国飞驰集团,Pulverisette 6系列行星式球磨机,其单位能耗为1.2J/c,c为行星式球磨机运行时所转动的圈数;其他参数为变量,如τ、N、T,根据实际需求,三者之间进行配合调整,例如,在一些具体的实施例中,选用内径5cm、容积50ml的氧化锆罐,球磨机内磨球的直径为1cm,磨球材质为氧化锆,本方案中,行星磨的转速为200-600r/min,合适但非限制性地,例如200r/min、300r/min、400r/min、500r/min、600r/min,球料比为15:1、20:1或30:1,活化时间为10-120min,合适但非限制性地,例如,10min、20min、30min、40min、50min、80min、90min、120min,由于机械活化充能过大,超过了淀粉可承受阈值,则淀粉结构被破坏,降低抑制剂的效果,机械活化充能过低,达不到淀粉活化的目的,因此,本方案中,各机械活化条件所确定的机械活化充能能量范围为:2.6KJ-32KJ,以所设定的机械活化充能能量范围为基准,调整三个变量参数的数值,通过充能能量公式(Ⅰ)计算得到不同条件下的充能能量值E;It is worth noting that in the charging energy formula (I), f is the starch activation constant, which refers to the conversion efficiency of different starches for mechanical activation and charging, which is determined by the properties of each starch itself. For example, the starch constant f of ordinary corn is 1.26 ; e i is the unit energy consumption of the planetary mill, which is obtained through the power conversion of the selected planetary mill instrument. In this application, the used planetary mill is the German Feichi Group, Pulverisette 6 series planetary ball mill, and its unit energy consumption is 1.2 J/c, c is the number of circles that the planetary ball mill rotates during operation; other parameters are variables, such as τ, N, T, and are adjusted according to actual needs, for example, in some specific embodiments , select a zirconia jar with an inner diameter of 5cm and a volume of 50ml, the diameter of the ball mill in the ball mill is 1cm, and the material of the ball is zirconia. In this scheme, the rotational speed of the planetary mill is 200-600r/min, which is suitable but not restrictive. For example 200r/min, 300r/min, 400r/min, 500r/min, 600r/min, the ball-to-material ratio is 15:1, 20:1 or 30:1, the activation time is 10-120min, suitable but not limited , for example, 10min, 20min, 30min, 40min, 50min, 80min, 90min, 120min, due to excessive mechanical activation charging, exceeding the threshold value of starch tolerance, the starch structure will be destroyed, reducing the effect of inhibitors, mechanical activation charging If it is too low, the purpose of starch activation cannot be achieved. Therefore, in this plan, the range of mechanical activation charging energy determined by each mechanical activation condition is: 2.6KJ-32KJ, based on the set mechanical activation charging energy range , adjust the values of the three variable parameters, and calculate the charging energy value E under different conditions through the charging energy formula (Ⅰ);

以普通玉米淀粉为例,按照上述步骤得到的回收率-充能公式,为:ε=0.002E2-0.043E+0.24,通过上述公式取极值,浮选回收率为1%,充能E为10.75KJ,淀粉抑制剂效果最佳,即机械活化淀粉最佳输入能量为10.75KJ,通过充能能量公式(Ⅰ)可确定的最优机械活化条件之一为:转速400r/min、活化时间为20min、球料比为15:1,为验证公式的准确性,得到回收率-充能公式以确定机械活化淀粉最佳输入能量,得到高活性的淀粉抑制剂,将该淀粉抑制剂应用于本方案的赤铁矿的浮选实验中,在低浓度抑制剂用量下得到的赤铁矿浮选回收率为<1%,说明本方法所提供的公式准确性高;Taking ordinary cornstarch as an example, the recovery rate-charging formula obtained according to the above steps is: ε=0.002E 2 -0.043E+0.24, by taking the extreme value of the above formula, the flotation recovery rate is 1%, and the charging E is 10.75KJ, the effect of starch inhibitor is the best, that is, the optimal input energy for mechanical activation of starch is 10.75KJ, and one of the optimal mechanical activation conditions that can be determined by charging energy formula (I) is: rotation speed 400r/min, activation time For 20min, the pellet ratio is 15:1. In order to verify the accuracy of the formula, the recovery rate-charging formula is obtained to determine the optimal input energy of mechanically activated starch, and a highly active starch inhibitor is obtained. The starch inhibitor is applied to In the flotation experiment of the hematite of this scheme, the hematite flotation recovery rate obtained under the low-concentration inhibitor dosage is <1%, which shows that the formula provided by this method has high accuracy;

本申请提供一种机械活化淀粉抑制剂。The present application provides a mechanically activated starch inhibitor.

本申请提供一种机械活化淀粉抑制剂在矿物分选效率中的应用,矿物包括赤铁矿、重晶石、高岭石等中的一种或几种,使得部分矿物可浮性下降,以扩大不同矿物间的可浮性差异,应用的步骤如下:以得到的淀粉抑制剂为溶质,去离子水为溶剂,配置成0.8g/L淀粉抑制剂溶液;以上述淀粉抑制剂溶液为抑制剂对不同的矿物进行浮选分离,包括以下步骤(赤铁矿浮选为例):将2g赤铁矿(200-400目)加入浮选槽,加入25ml去离子水搅拌2min,形成矿浆,将矿浆的pH调整至10,搅拌2min,加入机械活化淀粉抑制剂的水溶液(2ml),使浮选槽内淀粉抑制剂浓度为40mg/L,搅拌2min后,再加入1mL 1.6g/L十二胺捕收剂,搅拌2min,再加入2滴起泡剂,经浮选刮泡,将槽内矿物过滤、烘干、称重,记录称重数据,回收率为槽内精矿质量与所称取的待浮选矿样的质量比,计算得出对应的选矿回收率,即可分析淀粉抑制剂效果。This application provides an application of a mechanically activated starch inhibitor in mineral sorting efficiency. Minerals include one or more of hematite, barite, kaolinite, etc., which reduces the buoyancy of some minerals, and To expand the difference in floatability between different minerals, the application steps are as follows: use the obtained starch inhibitor as the solute and deionized water as the solvent to prepare a 0.8g/L starch inhibitor solution; use the above starch inhibitor solution as the inhibitor Different minerals are separated by flotation, including the following steps (hematite flotation as an example): add 2g hematite (200-400 mesh) into the flotation cell, add 25ml deionized water and stir for 2min to form a slurry, and put Adjust the pH of the pulp to 10, stir for 2 minutes, add an aqueous solution (2ml) of mechanically activated starch inhibitor to make the concentration of the starch inhibitor in the flotation tank 40mg/L, stir for 2min, then add 1mL of 1.6g/L dodecylamine Collecting agent, stirred for 2 minutes, then added 2 drops of foaming agent, after flotation and scraping, the minerals in the tank were filtered, dried, weighed, and the weighing data was recorded. The recovery rate was equal to the weight of the concentrate in the tank and the The mass ratio of the ore sample to be flotation is calculated to obtain the corresponding recovery rate of ore dressing, and then the effect of starch inhibitor can be analyzed.

以下结合具体实施例对本方案进行进一步说明。The scheme will be further described below in conjunction with specific examples.

实施例1Example 1

一种优化机械活化淀粉抑制剂的活化方法,包括以下步骤:An activation method for optimizing mechanically activated starch inhibitors, comprising the following steps:

S1.机械活化淀粉抑制剂制备及充能能量的计算S1. Preparation of Mechanically Activated Starch Inhibitor and Calculation of Charging Energy

称取4g玉米淀粉(NS),放置于行星磨氧化锆罐内备用;Take by weighing 4g cornstarch (NS), be placed in the planetary mill zirconia tank for subsequent use;

分别按实验组1-5所设定的行星磨参数对淀粉原料进行干法机械活化:以活化时间为变量,室温下使用行星磨在转速400r/min条件下将玉米淀粉(NS)分别机械活化10min、15min、25min、30min、60min,磨球和玉米淀粉(NS)球料比为15:1,机械球磨过程结束后,按照充能能量公式(Ⅰ)计算对应的充能能量值:According to the planetary mill parameters set by the experimental group 1-5, the dry mechanical activation of the starch raw materials was carried out: the activation time was used as a variable, and the corn starch (NS) was mechanically activated by the planetary mill at room temperature at a speed of 400r/min. 10min, 15min, 25min, 30min, 60min, the ratio of grinding balls to cornstarch (NS) balls is 15:1, after the mechanical ball milling process, calculate the corresponding charging energy value according to the charging energy formula (I):

Figure BDA0003879671400000081
Figure BDA0003879671400000081

其中,E为充能能量、f为淀粉活化指数、τ为球料比、ei为行星磨的单位能耗、N为行星磨转速、T为活化时间,f、ei为常量,f为玉米淀粉(NS)活化指数,其值为1.26,ei为行星磨的单位能耗,其值为1.2J/c,按照实验组1-5所设定的不同的球料比、活化时间、行星磨转速,得到不同的普通玉米活化淀粉抑制剂,计算得充能能量分别为5.376KJ、8.064KJ、13.44KJ、16.128KJ、32.256KJ的机械活化玉米淀粉(NS),本实施例中,氧化锆罐内径4cm,容积50ml;氧化锆罐内磨球的直径为1cm,磨球材料为氧化锆材质。Among them, E is the charging energy, f is the starch activation index, τ is the ball-to-material ratio, e i is the unit energy consumption of the planetary mill, N is the rotational speed of the planetary mill, T is the activation time, f and e i are constants, and f is Cornstarch (NS) activation index, its value is 1.26, e i is the unit energy consumption of planetary mill, its value is 1.2J/c, according to the different ball-to-material ratios set by experimental groups 1-5, activation time, Rotating speed of planetary mill, different common corn activated starch inhibitors are obtained, the calculated charging energy is respectively 5.376KJ, 8.064KJ, 13.44KJ, 16.128KJ, 32.256KJ mechanically activated cornstarch (NS), in the present embodiment, oxidation The inner diameter of the zirconium tank is 4cm, and the volume is 50ml; the diameter of the grinding ball in the zirconia tank is 1cm, and the material of the grinding ball is zirconia.

S2.浮选试验,记录实验数据S2. Flotation test, record experimental data

将步骤S1得到的不同的普通玉米活化淀粉抑制剂按照矿物浮选实验,并进行回收率测试,得到回收率ε,浮选实验步骤如下:The different ordinary corn activated starch inhibitors obtained in step S1 are tested according to the mineral flotation test, and the recovery rate is tested to obtain the recovery rate ε. The flotation test steps are as follows:

称取0.08g淀粉以去离子水为溶剂,配置成0.8g/L淀粉抑制剂溶液;以上述淀粉抑制剂溶液为抑制剂对不同的矿物进行浮选分离,包括以下步骤(赤铁矿浮选为例):将2g赤铁矿(200-400目)加入浮选槽,加入25ml去离子水搅拌2min,形成矿浆,将矿浆的pH调整至10,搅拌2min,加入机械活化淀粉抑制剂的水溶液(2ml),使浮选槽内淀粉抑制剂浓度为40mg/L,搅拌2min后,再加入1mL 1.6g/L十二胺捕收剂,搅拌2min,再加入2滴起泡剂,经浮选刮泡,将槽内矿物过滤、烘干、称重,记录称重数据,回收率为槽内精矿质量与所称取的待浮选矿样的质量比,计算得出对应的浮选回收率,结果如图1所示。Take by weighing 0.08g starch and take deionized water as solvent, configure 0.8g/L starch inhibitor solution; Use above-mentioned starch inhibitor solution as inhibitor to carry out flotation separation to different minerals, comprise the following steps (hematite flotation For example): add 2g hematite (200-400 mesh) into the flotation cell, add 25ml deionized water and stir for 2 minutes to form a slurry, adjust the pH of the slurry to 10, stir for 2 minutes, add the aqueous solution of mechanically activated starch inhibitor (2ml), so that the starch inhibitor concentration in the flotation tank is 40mg/L, after stirring for 2min, add 1mL of 1.6g/L dodecylamine collector, stir for 2min, then add 2 drops of foaming agent, after flotation Scrape, filter, dry, and weigh the minerals in the tank, record the weighing data, the recovery rate is the mass ratio of the concentrate mass in the tank to the weighed ore sample to be flotation, and calculate the corresponding flotation recovery rate, and the results are shown in Figure 1.

S3.SPSS拟合回收率与充能数据,得到回收率-充能公式S3.SPSS fits the recovery rate and charging data to obtain the recovery rate-charging formula

将步骤S1中的参数以及不同参数条件下计算得到的充能能能量(E)、步骤S2对应记录的浮选回收率(ε)整理得到表1:The parameters in step S1, the charging energy (E) calculated under different parameter conditions, and the flotation recovery rate (ε) corresponding to the records in step S2 are sorted out to obtain Table 1:

表1玉米淀粉(NS)抑制剂的参数The parameter of table 1 corn starch (NS) inhibitor

类别category 项目数number of items ττ N(r/min)N(r/min) T(min)T(min) E(J)E(J) ε(%)ε(%) 实验组1Experimental group 1 11 1515 400400 1010 53765376 1919 实验组2Experimental group 2 22 1515 400400 1515 80648064 99 实验组3Experimental group 3 33 1515 400400 2525 1344013440 88 实验组4Experimental group 4 44 1515 400400 3030 1612816128 1616 实验组5Experimental group 5 55 1515 400400 6060 322560322560 22twenty two 拟合最优组best fit group 66 1515 400400 2020 1075210752 11

将上述数据中充能能能量(E)与浮选回收率(ε)经SPSS拟合,结果如图4所示,得到普通玉米活化淀粉的抑制回收率与充能能量的拟合关系式为:ε=0.002E2-0.043E+0.24,即为普通玉米淀粉回收率-充能公式,拟合优度R2=0.98,拟合优度R2≥0.9。The charging energy energy (E) and the flotation recovery rate (ε) in the above data were fitted by SPSS, and the results are shown in Figure 4. The fitting relationship between the inhibition recovery rate and the charging energy of common corn activated starch was obtained as : ε=0.002E 2 -0.043E+0.24, which is the general corn starch recovery rate-charging formula, goodness of fit R 2 =0.98, goodness of fit R 2 ≥0.9.

S4.确定最佳充能能量值Ei及最佳机械活化参数集合,S4. Determine the optimal charging energy value E i and the optimal mechanical activation parameter set,

S5.基于最佳机械活化参数集合,制备机械活化淀粉抑制剂。S5. Based on the optimal set of mechanical activation parameters, prepare a mechanically activated starch inhibitor.

通过回收率-充能公式,求导取极值得到最佳充能能量值为10750KJ,本实施例中,仅活化时间为变量,球料比与行星磨转速为定量,带入充能能量公式(Ⅰ)计算,得到最佳机械活化时间为20min。。Through the recovery rate-charging formula, deriving the extreme value to obtain the optimal charging energy value is 10750KJ. In this embodiment, only the activation time is a variable, and the ball-to-material ratio and planetary mill speed are quantitative, which is brought into the charging energy formula (I) calculation, the best mechanical activation time is 20min. .

验证公式的有效性Verify the validity of the formula

按照步骤S4确定的最佳机械活化参数集合制备机械活化淀粉抑制剂,并将该淀粉活化抑制剂进行浮选实验,浮选回收率为1%,淀粉抑制剂效果最佳,说明本方法的准确性高,上述拟合最优组中的参数组合即为最佳机械活化参数集合的组合。Prepare the mechanically activated starch inhibitor according to the optimal mechanical activation parameter set determined in step S4, and carry out the flotation experiment with the starch activated inhibitor. The performance is high, and the parameter combination in the above-mentioned optimal fitting group is the combination of the best mechanical activation parameter set.

实施例2Example 2

一种优化机械活化淀粉抑制剂的活化方法,包括以下步骤:An activation method for optimizing mechanically activated starch inhibitors, comprising the following steps:

S1.机械活化淀粉抑制剂制备及充能能量的计算S1. Preparation of Mechanically Activated Starch Inhibitor and Calculation of Charging Energy

称取4g玉米淀粉(NS),放置于行星磨氧化锆罐内备用;Take by weighing 4g cornstarch (NS), be placed in the planetary mill zirconia tank for subsequent use;

分别按实验组6-11所设定的行星磨参数对淀粉原料进行干法机械活化:以行星磨转速为变量,室温下使用行星磨在球磨时间20min条件下,分别在转速200r/min、300r/min、350r/min、450r/min、500r/min、600r/min条件下将玉米淀粉(NS)机械活化20min,磨球和玉米淀粉(NS)球料比为15:1,机械球磨过程结束后,按照充能能量公式(Ⅰ)计算对应的充能能量值:According to the planetary mill parameters set by the experimental group 6-11, the dry mechanical activation of the starch raw materials was carried out: the speed of the planetary mill was used as a variable, and the planetary mill was used at room temperature under the condition of a ball milling time of 20 minutes, respectively at a speed of 200r/min, 300r Under the conditions of /min, 350r/min, 450r/min, 500r/min, 600r/min, mechanically activate the corn starch (NS) for 20 minutes, the ratio of balls to corn starch (NS) is 15:1, and the mechanical ball milling process is over After that, calculate the corresponding charging energy value according to the charging energy formula (I):

Figure BDA0003879671400000101
Figure BDA0003879671400000101

其中,E为充能能量、f为淀粉活化指数、τ为球料比、ei为行星磨的单位能耗、N为行星磨转速、T为活化时间,f、ei为常量,f为玉米淀粉(NS)活化指数,其值为1.26,ei为行星磨的单位能耗,其值为1.2J/c,按照实验组6-11所设定的不同的球料比、活化时间、行星磨转速,得到不同的普通玉米活化淀粉抑制剂,计算得充能能量分别为5.376KJ、8.064KJ、10.752KJ、13.440KJ、16.128KJ的机械活化玉米淀粉(NS),本实施例中,氧化锆罐内径4cm,容积50ml;氧化锆罐内磨球的直径为1cm,磨球材料为氧化锆材质。Among them, E is the charging energy, f is the starch activation index, τ is the ball-to-material ratio, e i is the unit energy consumption of the planetary mill, N is the rotational speed of the planetary mill, T is the activation time, f and e i are constants, and f is Corn starch (NS) activation index, its value is 1.26, e i is the unit energy consumption of the planetary mill, its value is 1.2J/c, according to the different ball-to-material ratios set by experimental group 6-11, activation time, Rotating speed of planetary mill, different common corn activated starch inhibitors are obtained, the calculated charging energy is respectively 5.376KJ, 8.064KJ, 10.752KJ, 13.440KJ, 16.128KJ mechanically activated cornstarch (NS), in the present embodiment, oxidation The inner diameter of the zirconium tank is 4cm, and the volume is 50ml; the diameter of the grinding ball in the zirconia tank is 1cm, and the material of the grinding ball is zirconia.

S2.浮选试验,记录实验数据S2. Flotation test, record experimental data

将步骤S1得到的不同的普通玉米活化淀粉抑制剂按照矿物浮选实验,并进行回收率测试,得到回收率ε,浮选实验步骤如下:The different ordinary corn activated starch inhibitors obtained in step S1 are tested according to the mineral flotation test, and the recovery rate is tested to obtain the recovery rate ε. The flotation test steps are as follows:

称取0.08g淀粉以去离子水为溶剂,配置成0.8g/L淀粉抑制剂溶液;以上述淀粉抑制剂溶液为抑制剂对不同的矿物进行浮选分离,包括以下步骤(赤铁矿浮选为例):将2g赤铁矿(200-400目)加入浮选槽,加入25ml去离子水搅拌2min,形成矿浆,将矿浆的pH调整至10,搅拌2min,加入机械活化淀粉抑制剂的水溶液(2ml),使浮选槽内淀粉抑制剂浓度为40mg/L,搅拌2min后,再加入1mL 1.6g/L十二胺捕收剂,搅拌2min,再加入2滴起泡剂,经浮选刮泡,将槽内矿物过滤、烘干、称重,记录称重数据,回收率为槽内精矿质量与所称取的待浮选矿样的质量比,计算得出对应的浮选回收率,结果如图2所示。Take by weighing 0.08g starch and take deionized water as solvent, configure 0.8g/L starch inhibitor solution; Use above-mentioned starch inhibitor solution as inhibitor to carry out flotation separation to different minerals, comprise the following steps (hematite flotation For example): add 2g hematite (200-400 mesh) into the flotation cell, add 25ml deionized water and stir for 2 minutes to form a slurry, adjust the pH of the slurry to 10, stir for 2 minutes, add the aqueous solution of mechanically activated starch inhibitor (2ml), so that the starch inhibitor concentration in the flotation tank is 40mg/L, after stirring for 2min, add 1mL of 1.6g/L dodecylamine collector, stir for 2min, then add 2 drops of foaming agent, after flotation Scrape, filter, dry, and weigh the minerals in the tank, record the weighing data, the recovery rate is the mass ratio of the concentrate mass in the tank to the weighed ore sample to be flotation, and calculate the corresponding flotation recovery rate, and the results are shown in Figure 2.

S3.SPSS拟合回收率与充能数据,得到回收率-充能公式S3.SPSS fits the recovery rate and charging data to obtain the recovery rate-charging formula

将步骤S1中的参数以及不同参数条件下计算得到的充能能能量(E)、步骤S2对应记录的浮选回收率(ε)整理得到表2:The parameters in step S1, the charging energy (E) calculated under different parameter conditions, and the flotation recovery rate (ε) corresponding to the records in step S2 are sorted out to obtain Table 2:

表2玉米淀粉(NS)抑制剂的参数The parameter of table 2 corn starch (NS) inhibitor

类别category ττ N(r/min)N(r/min) T(min)T(min) E(J)E(J) ε(%)ε(%) 实验组1Experimental group 1 1515 200200 2020 53765376 1818 实验组2Experimental group 2 1515 300300 2020 80648064 99 实验组3Experimental group 3 1515 350350 2020 94089408 88 实验组4Experimental group 4 1515 450450 2020 1209612096 1010 实验组5Experimental group 5 1515 500500 2020 1344013440 1616 实验组6Experimental group 6 1515 600600 2020 1612816128 22twenty two 拟合最优组best fit group 1515 400400 2020 1075210752 11

将上述数据中充能能能量(E)与浮选回收率(ε)经SPSS拟合,结果如图4所示,得到普通玉米活化淀粉的抑制回收率与充能能量的拟合关系式为:ε=0.002E2-0.043E+0.24,即为普通玉米淀粉回收率-充能公式,拟合优度R2=0.98,拟合优度R2≥0.9。The charging energy energy (E) and the flotation recovery rate (ε) in the above data were fitted by SPSS, and the results are shown in Figure 4. The fitting relationship between the inhibition recovery rate and the charging energy of common corn activated starch was obtained as : ε=0.002E 2 -0.043E+0.24, which is the general corn starch recovery rate-charging formula, goodness of fit R 2 =0.98, goodness of fit R 2 ≥0.9.

S4.确定最佳充能能量值Ei及最佳机械活化参数集合S4. Determine the optimal charging energy value E i and the optimal mechanical activation parameter set

通过回收率-充能公式,求导取极值得到最佳充能能量值为10750KJ,本实施例中,仅行星磨转速为变量,球料比与活化时间为定量,带入充能能量公式(Ⅰ)计算,得到最佳行星式球磨机转速为400r/min。Through the recovery rate-charging formula, deriving the extreme value to obtain the optimal charging energy value is 10750KJ. In this embodiment, only the rotation speed of the planetary mill is a variable, and the ball-to-material ratio and activation time are quantitative, which is brought into the charging energy formula (I) calculation, the best planetary ball mill speed is 400r/min.

S5.基于最佳机械活化参数集合,制备机械活化淀粉抑制剂。S5. Based on the optimal set of mechanical activation parameters, prepare a mechanically activated starch inhibitor.

验证公式的有效性Verify the validity of the formula

按照步骤S4确定的最佳机械活化参数集合制备机械活化淀粉抑制剂,并将该淀粉活化抑制剂进行浮选实验,浮选回收率为1%,淀粉抑制剂效果最佳,说明本方法的准确性高,上述拟合最优组1中的参数组合即为最佳机械活化参数集合的组合Prepare the mechanically activated starch inhibitor according to the optimal mechanical activation parameter set determined in step S4, and carry out the flotation experiment with the starch activated inhibitor. High performance, the parameter combination in the above-mentioned optimal fitting group 1 is the combination of the best mechanical activation parameter set

实施例3Example 3

一种优化机械活化淀粉抑制剂的活化方法,包括以下步骤:An activation method for optimizing mechanically activated starch inhibitors, comprising the following steps:

S1.机械活化淀粉抑制剂制备及充能能量的计算S1. Preparation of Mechanically Activated Starch Inhibitor and Calculation of Charging Energy

称取4g玉米淀粉(NS),放置于行星磨氧化锆罐内备用;Take by weighing 4g cornstarch (NS), be placed in the planetary mill zirconia tank for subsequent use;

分别按实验组12-15所设定的行星磨参数对淀粉原料进行干法机械活化:以球料比为变量,室温下使用行星磨在转速400r/min条件下将玉米淀粉(NS)机械活化20min,磨球和玉米淀粉(NS)球料比为10:1、20:1、30:1,机械球磨过程结束后,按照充能能量公式(Ⅰ)计算对应的充能能量值:Carry out dry mechanical activation of starch raw materials according to the planetary mill parameters set by experimental groups 12-15: use the ball-to-material ratio as a variable, use a planetary mill at room temperature to mechanically activate corn starch (NS) at a speed of 400r/min For 20 minutes, the ball-to-material ratio of grinding balls and cornstarch (NS) is 10:1, 20:1, 30:1. After the mechanical ball milling process, calculate the corresponding charging energy value according to the charging energy formula (Ⅰ):

Figure BDA0003879671400000121
Figure BDA0003879671400000121

其中,E为充能能量、f为淀粉活化指数、τ为球料比、ei为行星磨的单位能耗、N为行星磨转速、T为活化时间,f、ei为常量,f为玉米淀粉(NS)活化指数,其值为1.26,ei为行星磨的单位能耗,其值为1.2J/c,按照实验组12-15所设定的不同的球料比、活化时间、行星磨转速,得到不同的普通玉米活化淀粉抑制剂,计算得充能能量分别为10.842KJ、10.584KJ、10.416KJ的机械活化玉米淀粉(NS),本实施例中,氧化锆罐内径4cm,容积50ml;氧化锆罐内磨球的直径为1cm,磨球材料为氧化锆材质。Among them, E is the charging energy, f is the starch activation index, τ is the ball-to-material ratio, e i is the unit energy consumption of the planetary mill, N is the rotational speed of the planetary mill, T is the activation time, f and e i are constants, and f is Cornstarch (NS) activation index, its value is 1.26, e i is the unit energy consumption of planetary mill, its value is 1.2J/c, according to the different ball-to-material ratios set by experimental group 12-15, activation time, Planetary mill speed, different common corn activated starch inhibitors are obtained, and the calculated charging energy is respectively 10.842KJ, 10.584KJ, 10.416KJ mechanically activated cornstarch (NS). In this embodiment, the inner diameter of the zirconia tank is 4cm, and the volume 50ml; the diameter of the grinding ball in the zirconia tank is 1cm, and the material of the grinding ball is zirconia.

S2.浮选试验,记录实验数据S2. Flotation test, record experimental data

将步骤S1得到的不同的普通玉米活化淀粉抑制剂按照矿物浮选实验,并进行回收率测试,得到回收率ε,浮选实验步骤如下:The different ordinary corn activated starch inhibitors obtained in step S1 are tested according to the mineral flotation test, and the recovery rate is tested to obtain the recovery rate ε. The flotation test steps are as follows:

称取0.08g淀粉以去离子水为溶剂,配置成0.8g/L淀粉抑制剂溶液;以上述淀粉抑制剂溶液为抑制剂对不同的矿物进行浮选分离,包括以下步骤(赤铁矿浮选为例):将2g赤铁矿(200-400目)加入浮选槽,加入25ml去离子水搅拌2min,形成矿浆,将矿浆的pH调整至10,搅拌2min,加入机械活化淀粉抑制剂的水溶液(2ml),使浮选槽内淀粉抑制剂浓度为40mg/L,搅拌2min后,再加入1mL 1.6g/L十二胺捕收剂,搅拌2min,再加入2滴起泡剂,经浮选刮泡,将槽内矿物过滤、烘干、称重,记录称重数据,回收率为槽内精矿质量与所称取的待浮选矿样的质量比,计算得出对应的浮选回收率,结果如图3所示。Take by weighing 0.08g starch and take deionized water as solvent, configure 0.8g/L starch inhibitor solution; Use above-mentioned starch inhibitor solution as inhibitor to carry out flotation separation to different minerals, comprise the following steps (hematite flotation For example): add 2g hematite (200-400 mesh) into the flotation cell, add 25ml deionized water and stir for 2 minutes to form a slurry, adjust the pH of the slurry to 10, stir for 2 minutes, add the aqueous solution of mechanically activated starch inhibitor (2ml), so that the starch inhibitor concentration in the flotation tank is 40mg/L, after stirring for 2min, add 1mL of 1.6g/L dodecylamine collector, stir for 2min, then add 2 drops of foaming agent, after flotation Scrape, filter, dry, and weigh the minerals in the tank, record the weighing data, the recovery rate is the mass ratio of the concentrate mass in the tank to the weighed ore sample to be flotation, and calculate the corresponding flotation recovery rate, and the results are shown in Figure 3.

S3.SPSS拟合回收率与充能数据,得到回收率-充能公式S3.SPSS fits the recovery rate and charging data to obtain the recovery rate-charging formula

将步骤S1中的参数以及不同参数条件下计算得到的充能能能量(E)、步骤S2对应记录的浮选回收率(ε)整理得到表3:The parameters in step S1, the charging energy (E) calculated under different parameter conditions, and the flotation recovery rate (ε) corresponding to the records in step S2 are sorted out to obtain Table 3:

表3玉米淀粉(NS)抑制剂的参数The parameter of table 3 corn starch (NS) inhibitor

类别category ττ N(r/min)N(r/min) T(min)T(min) E(J)E(J) ε(%)ε(%) 实验组1Experimental group 1 1010 200200 2020 1084210842 1818 实验组2Experimental group 2 2020 300300 2020 1058410584 99 实验组3Experimental group 3 3030 350350 2020 1041610416 1616 拟合最优组best fit group 1515 400400 2020 1075210752 11

将上述数据中充能能能量(E)与浮选回收率(ε)经SPSS拟合,结果如图4所示,得到普通玉米活化淀粉的抑制回收率与充能能量的拟合关系式为:ε=0.002E2-0.043E+0.24,即为普通玉米淀粉回收率-充能公式,拟合优度R2=0.98,拟合优度R2≥0.9。The charging energy energy (E) and the flotation recovery rate (ε) in the above data were fitted by SPSS, and the results are shown in Figure 4. The fitting relationship between the inhibition recovery rate and the charging energy of common corn activated starch was obtained as : ε=0.002E 2 -0.043E+0.24, which is the general corn starch recovery rate-charging formula, goodness of fit R 2 =0.98, goodness of fit R 2 ≥0.9.

S4.确定最佳充能能量值Ei及最佳机械活化参数集合S4. Determine the optimal charging energy value E i and the optimal mechanical activation parameter set

通过回收率-充能公式,求导取极值得到最佳充能能量值为10750KJ,本实施例中,仅球料比为变量,活化时间与行星磨转速为定量,带入充能能量公式(Ⅰ)计算,得到最佳球料比为15:1。Through the recovery rate-charging formula, deriving the extreme value to obtain the optimal charging energy value is 10750KJ. In this embodiment, only the ball material ratio is a variable, and the activation time and planetary mill speed are quantitative, which is brought into the charging energy formula (I) calculation, the best ball-to-material ratio is 15:1.

综上实施例1-3,最佳机械活化条件为:机械活化时间20min、行星式球磨机转速400r/min、球料比15:1。To sum up the above examples 1-3, the optimal mechanical activation conditions are: mechanical activation time 20min, planetary ball mill speed 400r/min, ball-to-material ratio 15:1.

S5.基于最佳机械活化参数集合,制备机械活化淀粉抑制剂。S5. Based on the optimal set of mechanical activation parameters, prepare a mechanically activated starch inhibitor.

验证公式的有效性Verify the validity of the formula

按照步骤S4确定的最佳机械活化参数集合制备机械活化淀粉抑制剂,并将该淀粉活化抑制剂进行浮选实验,浮选回收率为1%,淀粉抑制剂效果最佳,说明本方法的准确性高,上述拟合最优组中的参数组合即为最佳机械活化参数集合的组合。Prepare the mechanically activated starch inhibitor according to the optimal mechanical activation parameter set determined in step S4, and carry out the flotation experiment with the starch activated inhibitor. The performance is high, and the parameter combination in the above-mentioned optimal fitting group is the combination of the best mechanical activation parameter set.

实施例4-6Example 4-6

通过改变淀粉原料为WS、G50、G80,重复上述步骤,得到WS最优机械活化时间是10min,最优行星式球磨机转速为400r/min,最优球料比为15:1;得到G50最优机械活化时间是20min,最优行星式球磨机转速为500r/min,最优球料比为15:1;得到G80最优机械活化时间是30min,最优行星式球磨机转速为400r/min,最优球料比为15:1。By changing the starch raw materials to WS, G50, and G80, and repeating the above steps, the optimal mechanical activation time of WS is 10 minutes, the optimal planetary ball mill speed is 400r/min, and the optimal ball-to-material ratio is 15:1; the optimal mechanical activation time of G50 is obtained. The mechanical activation time is 20min, the optimal planetary ball mill speed is 500r/min, and the optimal ball-to-material ratio is 15:1; the optimal mechanical activation time of G80 is 30min, the optimal planetary ball mill speed is 400r/min, the optimal The ball to material ratio is 15:1.

本申请通过对NS、WS、G50和G80经过较短时间的行星磨球磨机械活化,活化后的NST、WST、G50T和G80T化学反应活性提高,在浮选时与矿物的化学吸附能力提升,使矿物亲水并阻碍了矿物与捕收剂的结合,机械活化淀粉起到了抑制剂的作用,大大降低了浮选回收率。In this application, through the mechanical activation of NS, WS, G50 and G80 through planetary ball milling for a short period of time, the chemical reactivity of activated NST, WST, G50T and G80T is improved, and the chemical adsorption capacity with minerals is improved during flotation, so that Minerals are hydrophilic and hinder the combination of minerals and collectors, and mechanically activated starch acts as an inhibitor, which greatly reduces the recovery rate of flotation.

以上,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,可轻易想到的变化或替换,都应涵盖在本发明的保护范围之内。The above is only a preferred embodiment of the present invention, but the scope of protection of the present invention is not limited thereto, any changes or substitutions that can be easily conceived by those skilled in the art within the technical scope disclosed in the present invention, All should be covered within the protection scope of the present invention.

Claims (10)

1.一种优化机械活化淀粉抑制剂的活化方法,其特征在于,包括以下步骤:1. an activation method for optimizing mechanically activated starch inhibitor, is characterized in that, comprises the following steps: S1.以淀粉为原料,调整行星磨的机械活化参数集合,进行干法机械活化固相反应,以对淀粉原料进行充能,得到不同参数条件下的机械活化淀粉抑制剂,计算各机械活化淀粉抑制剂的充能能量值;S1. Using starch as a raw material, adjust the mechanical activation parameter set of the planetary mill, and perform a dry mechanical activation solid-phase reaction to charge the starch raw material, obtain mechanically activated starch inhibitors under different parameter conditions, and calculate each mechanically activated starch Inhibitor charge energy value; S2.以所述机械活化淀粉为抑制剂,分别对矿物进行浮选实验,并记录浮选回收率;S2. Using the mechanically activated starch as an inhibitor, carry out flotation experiments on minerals respectively, and record the flotation recovery rate; S3.通过SPSS拟合对应的充能能量值及浮选回收率,得到回收率-充能公式(Ⅱ),S3. Fit the corresponding charging energy value and flotation recovery rate through SPSS to obtain the recovery rate-charging formula (II), ε=αE2+βE+γ (Π),ε=αE 2 +βE+γ (Π), 其中ε为浮选回收率;α、β、γ为由淀粉种类确定的常数;Among them, ε is the flotation recovery rate; α, β, γ are constants determined by the type of starch; S4.通过回收率-充能公式(Ⅱ)计算最佳充能能量值Ei,将Ei带入充能能量公式(Ⅰ)中反推确定最佳机械活化参数集合;S4. Calculate the optimal charging energy value E i through the recovery rate-charging formula (II), and bring E i into the charging energy formula (I) to determine the optimal mechanical activation parameter set; S5.基于所述最佳机械活化参数集合,制备机械活化淀粉抑制剂。S5. Based on the optimal set of mechanical activation parameters, prepare a mechanically activated starch inhibitor. 2.根据权利要求1所述的优化机械活化淀粉抑制剂的活化方法,其特征在于,步骤S4中,最佳充能能量值Ei的计算方法为,将所述回收率-充能公式(Ⅱ)求导等于零,求解取极值即为最佳充能能量值Ei2. the activation method of optimization mechanically activated starch inhibitor according to claim 1, is characterized in that, in step S4, the computing method of optimal charging energy value E is , with described rate of recovery-charging formula ( Ⅱ) The derivation is equal to zero, and the extreme value of the solution is the optimal charging energy value E i . 3.根据权利要求1所述的优化机械活化淀粉抑制剂的活化方法,其特征在于,所述淀粉原料包括玉米淀粉、马铃薯淀粉、糯米淀粉、大米淀粉中的一种或几种。3. the activation method of optimization mechanically activated starch inhibitor according to claim 1, is characterized in that, described starch raw material comprises one or more in cornstarch, potato starch, glutinous rice starch, rice starch. 4.根据权利要求1所述的优化机械活化淀粉抑制剂的活化方法,其特征在于,步骤S4中,所述机械活化参数集合包括球料比、行星磨转速、活化时间三项参数;将所述最佳充能能量值Ei带入充能能量公式(Ⅰ)中,基于所述机械活化参数集合中的任意两项参数计算得到剩余一项参数,并将所获得的三项参数记为最佳机械活化参数集合。4. the activation method of optimization mechanical activation starch inhibitor according to claim 1, is characterized in that, in step S4, described mechanical activation parameter set comprises three parameters of ball material ratio, planetary mill rotating speed, activation time; The above optimal charging energy value E i is brought into the charging energy formula (I), and the remaining parameter is calculated based on any two parameters in the mechanical activation parameter set, and the obtained three parameters are recorded as Optimal set of mechanical activation parameters. 5.根据权利要求1所述的优化机械活化淀粉抑制剂的活化方法,其特征在于,步骤S1中,充能能量值的范围为2.6KJ-32KJ。5. The activation method for optimizing mechanically activated starch inhibitor according to claim 1, characterized in that, in step S1, the charging energy value ranges from 2.6KJ to 32KJ. 6.根据权利要求1所述的优化机械活化淀粉抑制剂的活化方法,其特征在于,所述浮选实验的步骤为,在待浮选的矿样中加入去离子水,并调整pH至碱性,加入所述机械活化淀粉抑制剂的水溶液,搅拌后,再加入捕收剂,搅拌、浮选刮泡,过滤槽内产物,烘干、称重,得浮选精矿的品位和回收率。6. the activation method of optimization mechanically activated starch inhibitor according to claim 1, is characterized in that, the step of described flotation experiment is, adds deionized water in the ore sample to be flotation, and adjusts pH to alkali properties, add the aqueous solution of the mechanically activated starch inhibitor, after stirring, then add the collector, stir, flotation scrape, filter the product in the tank, dry, weigh, and obtain the grade and recovery rate of the flotation concentrate . 7.根据权利要求1所述的优化机械活化淀粉抑制剂的活化方法,其特征在于,充能能量值由充能能量公式(Ⅰ)计算得到,7. the activation method of optimization mechanically activated starch inhibitor according to claim 1, is characterized in that, charging energy value is calculated by charging energy formula (I),
Figure FDA0003879671390000021
Figure FDA0003879671390000021
其中,E为充能能量、f为淀粉活化指数、τ为球料比、ei为行星磨的单位能耗、N为行星磨转速、T为活化时间。Among them, E is the charging energy, f is the starch activation index, τ is the pellet ratio, e i is the unit energy consumption of the planetary mill, N is the rotational speed of the planetary mill, and T is the activation time.
8.根据权利要求1-7任一项所述方法制备得到的机械活化淀粉抑制剂。8. The mechanically activated starch inhibitor prepared by the method according to any one of claims 1-7. 9.根据权利要求8所述的机械活化淀粉抑制剂在矿物分选中的应用。9. The application of the mechanically activated starch inhibitor according to claim 8 in mineral sorting. 10.根据权利要求9所述的应用,其特征在于,所述矿物包括赤铁矿、重晶石、高岭石中的一种或几种。10. The application according to claim 9, wherein the minerals include one or more of hematite, barite and kaolinite.
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