JPH03131302A - Porous filter for spray drying - Google Patents
Porous filter for spray dryingInfo
- Publication number
- JPH03131302A JPH03131302A JP1270101A JP27010189A JPH03131302A JP H03131302 A JPH03131302 A JP H03131302A JP 1270101 A JP1270101 A JP 1270101A JP 27010189 A JP27010189 A JP 27010189A JP H03131302 A JPH03131302 A JP H03131302A
- Authority
- JP
- Japan
- Prior art keywords
- porous filter
- spray drying
- filter
- porous
- air permeability
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000001694 spray drying Methods 0.000 title claims abstract description 36
- 238000001035 drying Methods 0.000 claims abstract description 25
- 230000035699 permeability Effects 0.000 claims abstract description 16
- 239000007921 spray Substances 0.000 claims description 6
- 239000000428 dust Substances 0.000 abstract description 15
- 239000000843 powder Substances 0.000 abstract description 15
- 238000005507 spraying Methods 0.000 description 6
- 239000000835 fiber Substances 0.000 description 5
- 229920001778 nylon Polymers 0.000 description 5
- 239000012528 membrane Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 4
- 239000004810 polytetrafluoroethylene Substances 0.000 description 4
- 239000004952 Polyamide Substances 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 229920002647 polyamide Polymers 0.000 description 3
- -1 polytetrafluoroethylene Polymers 0.000 description 3
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229920006389 polyphenyl polymer Polymers 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000011550 stock solution Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 1
- 239000004642 Polyimide Substances 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920001721 polyimide Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は噴霧乾燥装置の乾燥室に用いられる多孔質フィ
ルターに関する。更に、詳しくは噴霧乾燥装置の乾燥室
を構成し、生成粉粒体とガスとの分離を行なって粉粒体
を回収するための通気性の多孔質フィルターに関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a porous filter used in a drying chamber of a spray drying apparatus. More specifically, the present invention relates to an air-permeable porous filter that constitutes a drying chamber of a spray drying apparatus, separates produced powder from gas, and recovers the powder.
[従来の技術]
噴霧乾燥は、基本的には■原液の噴霧、■噴霧により生
じた微小液滴の乾燥、■粉粒体製品の分離回収の3つの
機能を必須としていたが、最近では、多品種少量生産方
式や高純度製品の製造が要請され、出願人は先に特開昭
62−152501公報において、噴霧、乾燥、分離回
収を同一の乾燥域で行うようにすると同時に、品種の切
り換えに応じ乾燥室を自在に取換えできる方法及び装置
を提案した。[Prior art] Spray drying basically requires three functions: ■ Spraying the stock solution, ■ Drying the minute droplets generated by spraying, and ■ Separating and collecting powdered products. In response to demands for a high-mix, low-volume production system and the manufacture of high-purity products, the applicant previously proposed in JP-A-62-152501 that spraying, drying, and separation and collection are performed in the same drying area, and at the same time, changing the product type. We proposed a method and device that allows the drying chamber to be freely replaced depending on the situation.
[発明が解決しようとする課題]
上記提案の方法及び装置は噴霧乾燥室を多孔質膜で構成
することにより、噴霧、乾燥、分離回収を同一の乾燥域
で行い、同時に乾燥室の取換えを容易にできるようにし
だものて、極めて実用性の高いものである。[Problems to be Solved by the Invention] The method and device proposed above configure the spray drying chamber with a porous membrane to perform spraying, drying, and separation and recovery in the same drying area, and at the same time, it is possible to replace the drying chamber. It is something that can be done easily and is highly practical.
本発明者は、この噴霧乾燥方法及び装置についてさらに
実験を重ねていたところ、熱風送風量、乾燥室の内外圧
力差、粉粒体の粒度などの運転条件如何により、乾燥室
を構成する多孔質膜、即ち多孔質フィルターからの粉塵
漏れが発生したり、圧力損失が大きくなり定常な運転が
できなくなるという事態に直面した。そこで本発明者は
、この原因究明と問題解決のため種々検討を行なった結
果、乾燥室を構成する多孔質フィルターの通気度あるい
は目開きを適切に選定すること、さらには運転時の多孔
質フィルターの形状(即ち、乾燥室の形状)を所定とす
ることで、上記問題を解決てきることを見出し、本発明
に到達したものである。As the inventor conducted further experiments on this spray drying method and apparatus, it was discovered that depending on the operating conditions such as the amount of hot air blown, the pressure difference between the inside and outside of the drying chamber, and the particle size of the powder or granular material, the porous structure constituting the drying chamber We were faced with a situation where dust leaked from the membrane, that is, a porous filter, and pressure loss increased, making steady operation impossible. Therefore, as a result of various studies to investigate the cause and solve the problem, the inventor of the present invention has found that it is necessary to appropriately select the air permeability or opening of the porous filter that constitutes the drying chamber, and furthermore, the porous filter during operation. The inventors have discovered that the above problem can be solved by setting the shape of the drying chamber (that is, the shape of the drying chamber) to a predetermined value, and have arrived at the present invention.
[課題を解決するための手段]
即ち、本発明によれば、噴霧乾燥装置の乾燥室を構成す
るフィルターであって、その通気度か0.5〜15 c
c/cm2/secである噴霧乾燥用多孔質フィルター
、および、噴霧乾燥装置の乾燥室を構成するフィルター
であって、その目開きか1〜100 μmである噴霧乾
燥用多孔質フィルターが提供される。[Means for Solving the Problems] That is, according to the present invention, there is provided a filter constituting a drying chamber of a spray drying device, which has an air permeability of 0.5 to 15 c.
Provided are a porous filter for spray drying that has a drying capacity of c/cm2/sec, and a porous filter for spray drying that constitutes a drying chamber of a spray drying device and has an opening of 1 to 100 μm. .
また、本発明ては、運転時の通気状態において、多孔質
フィルターの形状を、回転円盤型噴霧装置を採用する場
合は天井部が平面又は逆ロート状、圧力ノズル又は2流
体ノズルで噴霧する場合は天井部がロート状、側面部が
円筒状、底部がロート状を呈し、ロート状底部の傾斜角
度か30〜150°となるように形成する。このように
形成すれば、ロート状底部を下方から支持する必要もな
く好ましい。また、この形状は、多孔質フィルターの天
井部を噴霧乾燥装置のヘッド部(ここに、噴霧ノズル、
噴霧円盤等の噴霧手段が設置される。)と接続・固定し
、多孔質フィルターの底部を粉体取出口に接続・固定す
ることにより、常に安定して維持される。In addition, in the present invention, in the ventilation state during operation, the shape of the porous filter is changed such that when a rotating disk type spray device is used, the ceiling part is flat or inverted funnel shape, and when spraying is performed using a pressure nozzle or a two-fluid nozzle. The ceiling part is funnel-shaped, the side parts are cylindrical, and the bottom part is funnel-shaped, and the funnel-shaped bottom part is formed at an inclination angle of 30 to 150 degrees. If formed in this way, there is no need to support the funnel-shaped bottom from below, which is preferable. This shape also allows the ceiling of the porous filter to be connected to the head of the spray dryer (here, the spray nozzle,
A spraying means such as a spray disk is installed. ) and by connecting and fixing the bottom of the porous filter to the powder outlet, it is always maintained stably.
さらに、多孔質フィルターの縫い目が垂直方向となるよ
うに乾燥室全体を構成すると、縫い目を水平方向に形成
した場合のように縫い目付近に生成される粉粒体の堆積
が起こらず、多孔質フィルターに付着し難くなり好まし
い。なお、天井部においては、粉粒体は落下しやすいの
て縫い目の方向を限定する必要はない。Furthermore, if the entire drying chamber is configured so that the seams of the porous filter are vertical, the accumulation of powder and granules generated near the seams will not occur, unlike when the seams are formed horizontally, and the porous filter It is preferable because it is difficult to adhere to the surface. In addition, in the ceiling part, it is not necessary to limit the direction of the seams because the powder particles tend to fall.
[作用]
本発明の多孔質フィルターは、特定の範囲の通気度ある
いは目開きを有することに特徴がある。[Function] The porous filter of the present invention is characterized by having an air permeability or opening within a specific range.
噴霧乾燥装置の運転条件は、処理量の大小(即ち、装置
の大型、小型)、噴霧乾燥の対象原液の種類などにより
変化するものであるが、本発明者が種々実験、検討を行
なったところ、運転条件の広い範囲に亙って、特定の範
囲の通気度あるいは目開きを有する多孔質フィルターで
噴霧乾燥室を構成することにより、粉塵漏れが生じず、
安定した噴霧乾燥が行なえることを見出した。The operating conditions of the spray drying device vary depending on the amount of processing (i.e., large or small device), the type of stock solution to be spray dried, etc., but the inventor has conducted various experiments and studies. By configuring the spray drying chamber with a porous filter having a specific range of air permeability or opening over a wide range of operating conditions, no dust leakage occurs.
It has been found that stable spray drying can be performed.
本発明においては、多孔質フィルターの通気度を0 、
5〜15 cc/cm”/see、好ましくは1.0〜
8 cc/cm”/seeとする。この通気度の範囲は
、多孔質フィルターに強い付着又は堆積を形成させない
範囲てあり、噴霧乾燥装置の運転が安定する。特に、通
気度を低く安定させることで、多孔質フィルターへの粉
塵付着が抑えられ、かつ粉塵漏れを防止するのである。In the present invention, the air permeability of the porous filter is 0,
5 to 15 cc/cm”/see, preferably 1.0 to
8 cc/cm"/see. This air permeability range is within a range that does not form strong adhesion or deposits on the porous filter, and the operation of the spray drying equipment is stable. In particular, the air permeability should be kept low and stable. This prevents dust from adhering to the porous filter and prevents dust from leaking.
通気度が0 、5 cc/cm2/sec未満の場合に
は、噴霧乾燥運転に際して内外圧力差が大きくなり過ぎ
、安定した運転ができない。If the air permeability is less than 0.5 cc/cm2/sec, the difference in pressure between the inside and outside becomes too large during spray drying operation, making stable operation impossible.
方、通気度が15 cc/cm2/secを超えると、
多孔質フィルターからの粉塵漏れが生じる。On the other hand, if the air permeability exceeds 15 cc/cm2/sec,
Dust leaks from the porous filter.
また、本発明の多孔質フィルターの目開きについては、
基本的には粉粒体の形状・大きさに関係するものである
が、種々検討の結果、多孔質フィルターの目開きが1〜
1100B、好ましくは2〜50pmとすることにより
粉塵漏れが防止される。多孔質フィルターの目開きが1
7hm未満の場合、内外圧力差が大きくなり過ぎ安定し
た噴霧乾燥運転ができず、一方、目開きが100μmを
超えると粉塵漏れが生じる。Furthermore, regarding the opening of the porous filter of the present invention,
Basically, it is related to the shape and size of the powder, but as a result of various studies, we found that the opening of the porous filter is 1 to 1.
1100B, preferably 2 to 50 pm, prevents dust leakage. The opening of the porous filter is 1
When the opening is less than 7 hm, the difference between the inside and outside pressure becomes too large and stable spray drying operation cannot be performed. On the other hand, when the opening exceeds 100 μm, dust leakage occurs.
なお、上記の通気度、目開きは下記のように測定した。Note that the air permeability and mesh opening described above were measured as follows.
多孔質フィルターの通気度は、JIS L1096の
A法に基いて測定した。すなわち、フラジール形試験機
を用い、円筒の一端に試験片を取り付けた後、加減抵抗
器によって傾斜形気圧計が水柱1.27cm(124,
5Pa)の圧力を示すように吸込みファンを調整し、そ
のときの垂直形気圧計の示す圧力と、使用した空気孔の
種類とから、試験機に付属の表によって試験片を通過す
る空気量(cc/cm2/5ec)を求め、これを通気
度とした。The air permeability of the porous filter was measured based on method A of JIS L1096. That is, using a Frazier type tester, after attaching a test piece to one end of a cylinder, a rheostat was used to adjust the tilt type barometer to a height of 1.27 cm (124 cm) in the water column.
Adjust the suction fan so that it shows a pressure of 5 Pa), and from the pressure indicated by the vertical barometer and the type of air hole used, calculate the amount of air passing through the test piece ( cc/cm2/5ec) was determined, and this was taken as the air permeability.
多孔質フィルターの目開きは、顕微鏡下での計測により
求めた。濾材(フィルター)の間隙を通過てきる最大球
状粒子径を本発明では目開きとした。すなわち、観測て
きる目開きの短径部分の最大値を採用した。The opening of the porous filter was determined by measurement under a microscope. In the present invention, the maximum spherical particle diameter that can pass through the gaps of the filter medium is defined as the opening. In other words, the maximum value of the short axis portion of the eye opening that could be observed was adopted.
本発明に使用する多孔質フィルターは、耐熱性て且つ剥
離性に優れたものであることが好ましい。すなわち、噴
霧乾燥室内に導入される熱風温度は通常200〜280
°C程度と高温てあり、フィルターを通過する温度も5
0〜150℃であるため、これに耐えられるものてなく
てはならず、また、粉粒体か常に付着、堆積するから、
連続使用するためには良剥離性のものであることが望ま
しい。この多孔質フィルターは着脱自在に取付けられて
おり、随時取り替え可能となっている。そして、この多
孔質フィルターは対象となる製品粉粒体とガスとの分離
、即ち、粉粒体の回収を行なうものである。The porous filter used in the present invention is preferably heat resistant and has excellent removability. That is, the temperature of the hot air introduced into the spray drying chamber is usually 200 to 280.
It is as high as ℃, and the temperature that passes through the filter is 5℃.
Since the temperature is 0 to 150℃, it must be able to withstand this temperature, and powder and granules always adhere and accumulate, so
For continuous use, it is desirable to have good releasability. This porous filter is attached removably and can be replaced at any time. This porous filter separates the target product powder from the gas, that is, collects the powder.
このような機能を奏する多孔質フィルターとしては、特
にその種類を限定するものではないが、織布、不織布等
の繊維製の布やそれらの表面に多孔質フィルムを接合し
た組合せ膜が用いられる。As a porous filter that performs such a function, the type thereof is not particularly limited, but fibrous cloths such as woven cloth and nonwoven cloth, and combination membranes in which a porous film is bonded to the surface of these cloths are used.
多孔質フィルターの材質としては、耐熱ナイロン、ポリ
エステル、ポリイミド、ポリアミド、ポリフェニルサル
ファイド等が用いられる。また、多孔質フィルムとして
はポリテトラフルオロエチレン(PTFE)、ポリトリ
フルオロエチレン等が用いられる。次に、本発明の多孔
質フィルターを図面に基き説明する。As the material of the porous filter, heat-resistant nylon, polyester, polyimide, polyamide, polyphenyl sulfide, etc. are used. Moreover, polytetrafluoroethylene (PTFE), polytrifluoroethylene, etc. are used as the porous film. Next, the porous filter of the present invention will be explained based on the drawings.
第1図は運転時の本発明の多孔質フィルターの形状の一
例を示す説明図で、この例では天井部lは平面状て、図
示しない噴霧乾燥装置のヘッド部に接続・固定するため
の接続部2を有している。FIG. 1 is an explanatory diagram showing an example of the shape of the porous filter of the present invention during operation. In this example, the ceiling part l is flat and has a connection for connecting and fixing it to the head part of a spray drying device (not shown). It has part 2.
多孔質フィルターの側面部3は円筒状を呈するとともに
、底部4はロート状を呈しており、底部4はその下端部
5か図示しない噴霧乾燥装置の粉体取出口に接続・固定
されている。なお、多孔質フィルターの肩部、即ち天井
部1と側面部3の接続部分にはフック6か設けられ、噴
霧乾燥装置の上部固定部により吊り下げられる。The side surface 3 of the porous filter has a cylindrical shape, and the bottom 4 has a funnel shape, and the bottom 4 is connected and fixed to a lower end 5 of the powder outlet of a spray drying device (not shown). A hook 6 is provided at the shoulder of the porous filter, that is, at the connection between the ceiling 1 and the side surface 3, and is hung from the upper fixing part of the spray drying device.
また、乾燥室全体を構成する多孔質フィルターの縫い目
7を垂直方向となるように形成し、粉粒体の多孔質フィ
ルターへの付着を抑制した。Furthermore, the seams 7 of the porous filter constituting the entire drying chamber were formed in a vertical direction to suppress adhesion of the powder to the porous filter.
なお、ロート状底部4の傾斜角度αか30〜1506、
好ましくは50〜120’となるように形成すると、下
方からの支持手段を必要とせず上記形状を安定して保持
てきる。Incidentally, the inclination angle α of the funnel-shaped bottom portion 4 is 30 to 1506,
Preferably, when formed to have a length of 50 to 120', the above shape can be stably maintained without requiring support means from below.
」二足の如き多孔質フィルターの形状は、多孔質フィル
ターの内部の圧力を外部圧に対して通常1011111
H20以上とすることで保持される。The shape of the porous filter, such as a two-legged one, usually makes the internal pressure of the porous filter 1011111 relative to the external pressure.
It is maintained by setting it to H20 or higher.
[実施例]
以下、本発明を実施例に基いて更に詳細に説明するが、
本発明はこれらの実施例に限られるものではない。[Examples] The present invention will be explained in more detail based on Examples below.
The present invention is not limited to these examples.
(実施例)
各種繊維を用いた多孔質フィルターで乾燥室を構成し、
下記の条件で噴霧乾燥を行ない、フィルター特性および
フィルターからの粉塵漏れの有無を調べた。(Example) A drying chamber was constructed with a porous filter using various fibers,
Spray drying was performed under the following conditions, and the filter characteristics and the presence or absence of dust leakage from the filter were examined.
(噴霧乾燥条件)
■噴霧乾燥された粉粒体の平均粒子径
−−−10〜200 μm
■熱風入口温度・・・200〜250’C■送風量
=1000〜1500m’ /hr結果を第1表に示
す。(Spray drying conditions) ■Average particle diameter of spray-dried powder --- 10 to 200 μm ■Hot air inlet temperature...200 to 250'C ■Blow rate
=1000-1500 m'/hr The results are shown in Table 1.
第1表から明らかなように、特定範囲の通気度または目
開きを有する多孔質フィルターを用いた場合には、圧力
損失もそれ程大きくならない範囲て、粉塵漏れが防止で
きることがわかる。As is clear from Table 1, when a porous filter having an air permeability or opening within a specific range is used, dust leakage can be prevented within a range where the pressure loss does not become too large.
0
第1表
(註l)多孔質フィルターの材質
A・・・耐熱ナイロン繊維、B・・・耐熱ナイロン繊維
、C・・・耐熱ポリアミド繊維、D・・・ポリフェニル
サルファイド繊維、E・・・ポリテトラフルオロエチレ
ン(PTFE)(多孔質フィルム)と耐熱ナイロン繊維
の複合膜、F・・・耐熱ナイロン繊維、G・・・ポリフ
ェニルサルファイド繊維、H・・・耐熱ポリアミド繊維
(註2)粉塵漏れの有無
○・・・粉塵漏れ無し、×・・・粉塵漏れ有り(註3)
評価
■・・・特に良好、O・・・良好
1
[発明の効果]
以上説明した通り、本発明によれば、特定範囲の通気度
あるいは目開きを有する多孔質フィルターにより噴霧乾
燥装置の乾燥室を構成したのて、噴霧乾燥の運転条件の
如何に拘らず、安定した噴霧乾燥を行ないつつ多孔質フ
ィルターからの粉塵漏れを起こさないで粉粒体の回収を
行なうことがてきる。0 Table 1 (Notes) Material of porous filter A...Heat-resistant nylon fiber, B...Heat-resistant nylon fiber, C...Heat-resistant polyamide fiber, D...Polyphenyl sulfide fiber, E... Composite membrane of polytetrafluoroethylene (PTFE) (porous film) and heat-resistant nylon fiber, F...heat-resistant nylon fiber, G...polyphenylsulfide fiber, H...heat-resistant polyamide fiber (Note 2) Dust leakage Presence or absence○...No dust leakage, ×...Dust leakage (Note 3)
Evaluation ■: Particularly good, O: Good 1 [Effects of the invention] As explained above, according to the present invention, the drying chamber of the spray drying apparatus is With this structure, it is possible to perform stable spray drying and recover powder particles without causing dust leakage from the porous filter, regardless of the spray drying operating conditions.
第1図は運転時の本発明の多孔質フィルターの形状の一
例を示す説明図である。
1・・・多孔質フィルターの天井部、2・・・接続部、
3・・・多孔質フィルターの側面部、4・・・多孔質フ
ィルターの底部、5・・・下端部、6・・・フック、7
・・・縫い目。FIG. 1 is an explanatory diagram showing an example of the shape of the porous filter of the present invention during operation. 1... Ceiling part of the porous filter, 2... Connection part,
3... Side part of the porous filter, 4... Bottom part of the porous filter, 5... Lower end part, 6... Hook, 7
···stitch.
Claims (4)
って、その通気度が0.5〜15cc/cm^2/se
cであることを特徴とする噴霧乾燥用多孔質フィルター
。(1) A filter constituting the drying chamber of a spray dryer, whose air permeability is 0.5 to 15 cc/cm^2/se
A porous filter for spray drying, characterized in that c.
って、その目開きが1〜100μmであることを特徴と
する噴霧乾燥用多孔質フィルター。(2) A porous filter for spray drying, which is a filter constituting a drying chamber of a spray drying apparatus, and is characterized in that the opening thereof is 1 to 100 μm.
側面部が円筒状、底部がロート状を呈し、ロート状底部
の傾斜角度が30〜150゜である請求項1または2記
載の噴霧乾燥用多孔質フィルター。(3) The ceiling is flat, inverted funnel-shaped, or funnel-shaped;
3. The porous filter for spray drying according to claim 1, wherein the side part has a cylindrical shape, the bottom part has a funnel shape, and the funnel-shaped bottom part has an inclination angle of 30 to 150 degrees.
ている請求項3記載の噴霧乾燥用多孔質フィルター。(4) The porous filter for spray drying according to claim 3, wherein the seams of the porous filter are formed in a vertical direction.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27010189A JP3301610B2 (en) | 1989-10-17 | 1989-10-17 | Porous filter for spray drying |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27010189A JP3301610B2 (en) | 1989-10-17 | 1989-10-17 | Porous filter for spray drying |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03131302A true JPH03131302A (en) | 1991-06-04 |
JP3301610B2 JP3301610B2 (en) | 2002-07-15 |
Family
ID=17481550
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP27010189A Expired - Lifetime JP3301610B2 (en) | 1989-10-17 | 1989-10-17 | Porous filter for spray drying |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3301610B2 (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101223781B1 (en) * | 2012-07-03 | 2013-01-17 | 유영덕 | Stretching ceiling construction system and construction method thereof |
US8407912B2 (en) | 2010-09-16 | 2013-04-02 | Velico Medical, Inc. | Spray dried human plasma |
US8533971B2 (en) | 2010-10-29 | 2013-09-17 | Velico Medical, Inc. | System and method for spray drying a liquid |
US9867782B2 (en) | 2009-04-09 | 2018-01-16 | Entegrion, Inc. | Spray-dried blood products and methods of making same |
US10251911B2 (en) | 2009-09-16 | 2019-04-09 | Entegrion, Inc. | Spray dried human plasma |
US10843100B2 (en) | 2010-10-29 | 2020-11-24 | Velico Medical, Inc. | Spray drier assembly for automated spray drying |
US11052045B2 (en) | 2014-09-19 | 2021-07-06 | Velico Medical, Inc. | Formulations and methods for contemporaneous stabilization of active proteins during spray drying and storage |
US11841189B1 (en) | 2022-09-15 | 2023-12-12 | Velico Medical, Inc. | Disposable for a spray drying system |
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JPS521180A (en) * | 1975-06-20 | 1977-01-06 | Mitsubishi Rayon Co | Method of producing fabric for bag filter |
JPS5228862Y2 (en) * | 1972-03-30 | 1977-07-01 | ||
JPS5743212B2 (en) * | 1980-05-12 | 1982-09-13 | ||
JPS5888016A (en) * | 1981-11-19 | 1983-05-26 | Teijin Ltd | Heat resistant bag filter |
JPS62152501A (en) * | 1985-12-27 | 1987-07-07 | Tdk Corp | Spray drying method and apparatus |
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JPS5228862Y2 (en) * | 1972-03-30 | 1977-07-01 | ||
JPS521180A (en) * | 1975-06-20 | 1977-01-06 | Mitsubishi Rayon Co | Method of producing fabric for bag filter |
JPS6318420Y2 (en) * | 1979-04-10 | 1988-05-24 | ||
JPS5743212B2 (en) * | 1980-05-12 | 1982-09-13 | ||
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Cited By (16)
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---|---|---|---|---|
US9867782B2 (en) | 2009-04-09 | 2018-01-16 | Entegrion, Inc. | Spray-dried blood products and methods of making same |
US11213488B2 (en) | 2009-04-09 | 2022-01-04 | Entegrion, Inc. | Spray-dried blood products and methods of making same |
US10251911B2 (en) | 2009-09-16 | 2019-04-09 | Entegrion, Inc. | Spray dried human plasma |
US8407912B2 (en) | 2010-09-16 | 2013-04-02 | Velico Medical, Inc. | Spray dried human plasma |
US8434242B2 (en) | 2010-09-16 | 2013-05-07 | Velico Medical, Inc. | Spray dried human plasma |
US8533972B2 (en) | 2010-10-29 | 2013-09-17 | Velico Medical, Inc. | System and method for spray drying a liquid |
US8601712B2 (en) | 2010-10-29 | 2013-12-10 | Velico Medical, Inc. | System and method for spray drying a liquid |
US8595950B2 (en) | 2010-10-29 | 2013-12-03 | Velico Medical, Inc. | System and method for spray drying a liquid |
US10843100B2 (en) | 2010-10-29 | 2020-11-24 | Velico Medical, Inc. | Spray drier assembly for automated spray drying |
US8533971B2 (en) | 2010-10-29 | 2013-09-17 | Velico Medical, Inc. | System and method for spray drying a liquid |
KR101223781B1 (en) * | 2012-07-03 | 2013-01-17 | 유영덕 | Stretching ceiling construction system and construction method thereof |
US11052045B2 (en) | 2014-09-19 | 2021-07-06 | Velico Medical, Inc. | Formulations and methods for contemporaneous stabilization of active proteins during spray drying and storage |
US11806431B2 (en) | 2014-09-19 | 2023-11-07 | Velico Medical, Inc. | Formulations and methods for contemporaneous stabilization of active proteins during spray drying and storage |
US11841189B1 (en) | 2022-09-15 | 2023-12-12 | Velico Medical, Inc. | Disposable for a spray drying system |
US11913722B1 (en) | 2022-09-15 | 2024-02-27 | Velico Medical, Inc. | Rapid spray drying system |
US11913723B1 (en) | 2022-09-15 | 2024-02-27 | Velico Medical, Inc. | Baffle plate used in a disposable for a spray drying system |
Also Published As
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