Preparation method for rapid-disintegrating directly-pressed particle mannitol preparation

A technology of mannitol and granules, which is applied in the field of preparation of fast-collapsing direct-pressure granule mannitol preparations, can solve the problems of increased difficulty, low pass rate, and high manufacturing costs, and achieve easy operation and control, good product quality, and low manufacturing costs. low effect

Inactive Publication Date: 2012-07-18
DSM JIANGSHAN PHARMACEUTICAL (JIANGSU) CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the commonly used mannitol in the domestic market is needle-like crystals with poor fluidity. When tableting, it is often necessary to use more lubricants and glidants to help release the mold, thereby affecting the content and taste of the tablet, and the crystal structure is not easy to compress directly. , the dissolution rate is also slow
[0003] The existing granulated mannitol is mainly imported. It is obtained by heating mannitol or mannitol with a binder above the melting point to melt it into a liquid, and then cooling, agglomerating, pulverizing or extruding granules. Granular mannitol, this method has a high heating temperature, which is easy to cause the material to change color at high temperature, which affects the quality and use, and the melting time is difficult to grasp, the technical requirements are high, the operation control is difficult, the pass rate is low, the yield is low, the manufacturing cost is high, and the sales The price is also high
Another Guangxi Nanning patent number is CN200610019626.2 method: add 25%-35% water or water with a binder to the mannitol put into the mixer and mix it, and then input it into the rotary vacuum dryer after forming a mass , high-temperature and high-vacuum drying, and then cooling, crushing and sieving. This method is difficult to transfer materials. A large proportion of water is used to fuse and then dry, which consumes more energy. Large, the yield is not high, and the yield is not high. According to its introduction, the yield is only 50-60%, so the quality of the finished product is not stable

Method used

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  • Preparation method for rapid-disintegrating directly-pressed particle mannitol preparation
  • Preparation method for rapid-disintegrating directly-pressed particle mannitol preparation
  • Preparation method for rapid-disintegrating directly-pressed particle mannitol preparation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0009] Experiment with crushed mannitol:

[0010] Produce 99% granulated mannitol

[0011] formula:

[0012] Mannitol (pass 80 mesh crushing sieve) 1980g

[0013] Crospovidone 10g (internal addition)

[0014] Polyvinylpyrrolidone (K30) 10g (plus)

[0015] 1. Dissolve 10 g of polyvinylpyrrolidone (K30) in 260 g of purified water to prepare a binder slurry.

[0016] 2. Put 1980g of 80-mesh crushed mannitol and 10g of cross-linked povidone into a 4L high-speed stirring granulation pot, turn on the granulator, and add the prepared polyvinylpyrrolidone slurry for granulation. The way of low mixing and high cutting.

[0017] 3. Discharge after 240s of granulation and transfer to fluidized dryer for drying. After the material temperature is dried to 42℃, stop and discharge, use 20 mesh sieve to sieve, and the obtained upper sieve is sized on the rapid sizing machine with 20 mesh The granule sieve cage performs granulation, and then mixes to obtain the granule product.

[0018] 4. Test with 100 m...

Embodiment 2

[0023] Experiment with uncomminuted mannitol:

[0024] 99% granulated mannitol

[0025] formula:

[0026] Mannitol 1980g

[0027] Crospovidone 10g (internal addition)

[0028] Polyvinylpyrrolidone (K30) 10g (additional)

[0029] 1. Dissolve 10 g of polyvinylpyrrolidone (K30) in 240 g of purified water to prepare a binder slurry.

[0030] 2. Put 1980g of mannitol and 10g of cross-linked povidone into a 4L high-speed stirring granulation pot, turn on the granulator, add the prepared polyvinylpyrrolidone slurry for granulation, and use low agitation and high chopped the way.

[0031] 3. Discharge after 240s of granulation and transfer to fluidized dryer for drying. After the material temperature is dried to 42℃, stop and discharge, use 20 mesh sieve to sieve, and the obtained upper sieve is sized on the rapid sizing machine with 20 mesh The granule sieve cage performs granulation, and then mixes to obtain the granule product.

[0032] 4. Test with 100 mesh sieve, 22% under 100 mesh, bulk den...

Embodiment 3

[0036] Press directly with the uncomminuted crystal mannitol before:

[0037] formula:

[0038]

[0039] The pressed tablet has less luster, scratches and splits on the side, which also proves that the mannitol crystal alone does need to increase the lubricant, so the lubricant is added to 1.1%, but the hardness cannot be suppressed, ¢12mm round punch, Average tablet weight: 0.724g, hardness: 24N.

[0040] In summary, it can be seen that:

[0041] 1. Domestic mannitol is directly used for tableting, with poor quality and low hardness.

[0042] 2. The present invention directly improves this situation, can achieve a very high level of hardness and content, and can ensure the disintegration time limit of the American sublingual tablet, and broaden the application field of mannitol.

[0043] 3. The use of crushed mannitol can make the hardness higher, the melting point of mannitol is higher, and there is no melting and sticking phenomenon, so it is convenient to crush and can be finer. Un...

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Abstract

The invention relates to a preparation method for a rapid-disintegrating directly-pressed granular mannitol preparation. The preparation method comprises the following steps of: 1) weighing the following raw materials in percent by weight according to a particle mannitol formula: 0.2-5.0 percent of adhesive and 8-2 percent of purified water, pouring the adhesive into the purified water and preparing adhesive slurry for future use; 2) putting crushed or uncrushed mannitol and 0.2-5.0 percent of disintegrating agent in a high-speed agitating and granulating machine, starting up the high-speed agitating and granulating machine, adding the slurry and preparing high-quality soft materials; 3) transferring the product wet granules into a fluidized drying machine for drying, screening the dried materials and completely tidying the granules; and 4) mixing the screened and tidied materials with lubricating agent, pressing the mixture into tablets and conducting hardness and disintegration tests. By adopting the preparation method, widely applicable directly-pressed granules with different content and fineness can be produced, have a rapid disintegrating characteristic and satisfy the American standard that the disintegrating time of sublingual tablets is less than or equal to 30 seconds. Moreover, the preparation method has the advantages of easiness in operation, low production cost, simple technology and high product quality.

Description

Technical field: [0001] The invention relates to the technical field of health foods, in particular to a preparation method of a quick-disintegrating direct-pressure granular mannitol preparation. Background technique: [0002] Mannitol is a hexanol with a melting point of 166°C and a relative density of 1.52. 1g of this product is soluble in about 5.5ml of water (25°C) and more soluble in hot water. It absorbs heat when dissolved and has a sweet taste. It is comfortable to the oral cavity and has very low hygroscopicity, so it is more widely used in the manufacture of chewable tablets such as sobering medicines and mouth refreshing agents, and has a wide range of uses in the pharmaceutical and food fields. However, the commonly used mannitol in the domestic market is needle-like crystals, which has poor fluidity. It is often necessary to use more lubricants and glidants to help release the tablet during tablet compression, which affects the content and taste of the tablet, and t...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): A23L1/29A23L33/00
Inventor 张国栋倪国成卢鹏飞边立峰夏旭东
Owner DSM JIANGSHAN PHARMACEUTICAL (JIANGSU) CO LTD
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