
Arigo A et al /J. Pharm. Sci. & Res. Vol. 11(1), 2019, 6-10 Effect of Hygroscopicity on pharmaceutical ingredients, methods to determine and overcome: An Overview Arigo A1, Jawahar N1, Nikhitha K1, Jubie.S2 1Department of Pharmaceutics 2Department of Pharmaceutical chemistry, JSS College of Pharmacy, Ootacamund, India, 643001. JSS Academy of Higher Education and Research, Mysuru. Abstract The hygroscopic character of a pharmaceutical material is known to influence the behavior of the material during various stages of pharmaceutical process, manufacturing, packing, storage, and transport. It also influence greatly on the stability, appearance, efficiency of the materials. Hence it is important to classify and overcome the problems of the materials based on their hygroscopic nature. The following review covers the literature reports of classification, determination of hygroscopic materials based on their ability to absorb or adsorb water molecule from the environment. It also discuss about the effect of hygroscopicity due to uncontrolled humid conditions and basic methods to overcome the same. Keywords: hygroscopicity, stability, water in solids, moisture content, adsorption, desorption. INTRODUCTION crushing it. The material holds on tightly to the milling machine Hygroscopy is a chance of dragging and bonding with and resists during pneumatic conveyance. During tablet water molecule from the atmospheric air present at compounding, unwanted moisture retard appropriate reactions, surrounding environment at room temperature. Hygroscopicity is forms unwanted end products which results in minimum quality done by either absorption or adsorption of moisture from the and reduced shelf life. During powder flow, the capacity of the atmospheric air. Physically changed character of the material is powder materials to flow evenly is reduced due to enhanced due to the absorption or adsorption of moisture by the substance. moisture content. This is due to the enhancement of thickness of This could result in an increase in volume, boiling point, the adsorbed liquid layer. This in turn improves the stability or viscosity, or other physical characteristic or property of the firmness of liquid bridges formed between particles. Increased substance [30]. surface tension is due to the increased surface moisture, this The physical and chemical stability of the solid dosage concludes in attraction between particles [10-14]. forms, excipients, and polymers for controlled release In tablet Compression, compression of powdered formulations have been predominantly influenced by Moisture materials can be done under high pressure only in dry state. adsorption. The drugs which undergo hydrolysis by absorbing or Moisture causes clumping and caking, decomposes the drug, adsorbing the moisture form the environment. It is necessary to minimize the medicinal value and causes deterioration of the determine moisture adsorption kinetics which includes the rate of tableting process. During tablet Coating, inappropriate cooling moisture uptake, and also the equilibrium moisture content and drying of the sugar solution can conclude in rough, (EMC). Moisture adsorption principles will provide handy data in translucent and irregular coating [24]. case of solid dosage forms for selection of excipients, and also informations on humidity control required to be done during In Manufacturing production and storage. Influence in the flow, compression, and For Effervescent Tablets, uncontrolled moisture in the hardness of solid dosage forms is depend upon the quantity of manufacturing areas affects surface finish and result in softened moisture adsorbed by pharmaceutical materials at a particular tablets. While in cough drop, material adhere to the stamping temperature and relative humidity [3]. machine when humidity is high. Since aluminum is moisture The percent relative humidity (% RH) quantifies the sensitive in nature. It can result in penetration of moisture inside atmospheric water vapor pressure. The equilibrium moisture the packing during storage [24]. content (EMC) is defined as the quantity of moisture at which a solid material forms a water vapor pressure similar to the water In Packaging vapour present in the surrounding environment’s vapour pressure. At the time of Dry Powder filling / Vial filling, due to Moisture adsorbance rate are determined by the following factors: uncontrolled moisture powders get adhere to the conveyor, and 1) The pressure difference between the water vapor influence process of filling. pressure of the material and the vapor pressure of water During strip packaging, increased moisture content in in the atmosphere the atmospheric air present in the packaging area will eventually 2) A reaction constant related to the solid characteristic pave the way for the tablets and capsules to absorb moisture from 3) The water vapor of the exposed surface area of solid the environment thus decrease the shelf life. This may also reduce drug efficiency of the final materials [24]. 4) The speed of movement of moisture air 5) Temperature METHODS OF DETERMINATION The kinetics relays on the (a) surface adsorption, found to be Callahan and co-workers method (regular method present at a rate proportional to the gradient between the saturated Determinations of equilibrium moisture content is found salt solution and that of the partial pressure of water vapor in the by depositing exactly weighed sample (0.1-0.2 gram) in bare, atmosphere, and (b) the at which the diffusion of water into the weighed dish or bottle and then it is planted into a desiccator crystal that dependents on the concentration difference of water accommodating any of the following saturated salt solutions given and the product of the coefficient of diffusion [1,2]. in following table. A surplus volume of the saturated salt solution (with surplus crystals) (Table-1) is positioned in the pit of the EFFECT OF UNCONTROLLED HUMIDITY desiccator. Samples were stored in sealed desiccators, each In Processing containing a distinct moisture environment. At equilibrium (1 In Powder Milling, Water vapour makes material tough week storage at composed room temperature 250C ± 20C) the and challenging to reduce into small particles or powder by samples are detached from the desiccators and the change in 6 Arigo A et al /J. Pharm. Sci. & Res. Vol. 11(1), 2019, 6-10 moisture is found for each sample by procuring the resulting samples were then exposed to desorption ranging from 90% weight with the help of a weighing balance. Equilibrium moisture Relative Humidity to 0% Relative Humidity. The above process is content values were calculated from P (%moisture dry basis) with reproduced for another time from 0% Relative Humidity to 90% the help of the equations given below. Initial moisture content (A) Relative Humidity again falls back to 0% Relative Humidity. The of each excipient was accurately determined by a convenient percentage of weight changed at 25°C and 80% Relative method, such as loss on drying to stable and consistent weight and Humidity in the first adsorption cycle is established based on the employed to compute P. Equilibrium moisture content values are equation given below. The existence of difference between the computed from P with the aid of the formula given below[4,5] desorption and adsorption values is used to determine the A W B 100 characters of the sample. This is in terms of changes in solid state P = 100 occurred under the varying hygroscopicity determining condition A ��� W∗ W� − � ∗ � inside the sorption analyzer. Before and after carrying out the 100 sorption analysis, the sample is examined by powder X- ray EMC = [� −] � ∗ �� diffractometry (PXRD) in order to confirm the interpretations P Where, drawn from the sorption isotherm,. All diffraction patterns are P+100 P= percentage moisture dry basis gathered at a scan speed of 3°/min with a scan step of 0.02° over [4] W= initial sample weight in grams range of 3–45 °2Ө in continuous mode . A= Initial % moisture W2 + W1 % weight change = 100 B= Difference in weight at equilibrium in grams W1 Where, EMC= Equilibrium moisture content � � ∗ W1= sample weight at the initial time of the experiment Table-1: Saturated salt solutions for sustain Constant Relative W2= sample weight in equilibrium at 25°C and 80% Humidity conditions in desiccators Relative Humidity % Relative Humidity at Saturated salt solution Temperature 25˚C Karl Fischer Method Lithium Chloride 11 The Karl Fischer Method was constructed to find out Potassium Acetate 23 the amount of water content present in a substance. The Magnesium Chloride 33 quantitative reaction of water with iodine and sulfur dioxide in the Potassium Carbonate 43 presence of a lower alcohol and an organic base was utilized to Magnesium Nitrate 52 find out the amount of water content available in the substance. There are two varying methods of determination are available Sodium Nitrite 64 based on iodine-affording principle. One of them is volumetric Sodium Chloride 75 titration method and another one is coulometric titration method. Potassium Bromide 83 Iodine needed for reaction with water is formerly dissolved in Potassium Nitrate 93 sample Test Solution in case of the volumetric titration method, and the amount of iodine consumed as a result of reaction with European pharmacopoeia method water in a sample is used to measure the water content in the A surplus amount of saturated salt solution (with surplus sample. Initially the electrolysis of the reagent containing iodide crystals) of ammonium
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