JPH01194901A - Nozzle means and spray drier equipped therewith - Google Patents
Nozzle means and spray drier equipped therewithInfo
- Publication number
- JPH01194901A JPH01194901A JP1900888A JP1900888A JPH01194901A JP H01194901 A JPH01194901 A JP H01194901A JP 1900888 A JP1900888 A JP 1900888A JP 1900888 A JP1900888 A JP 1900888A JP H01194901 A JPH01194901 A JP H01194901A
- Authority
- JP
- Japan
- Prior art keywords
- nozzle
- pressure
- spray
- water
- cylindrical body
- 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
- 239000007921 spray Substances 0.000 title claims abstract description 29
- 238000007664 blowing Methods 0.000 claims abstract description 16
- 239000007788 liquid Substances 0.000 claims abstract description 6
- 238000001035 drying Methods 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 32
- 238000005507 spraying Methods 0.000 abstract description 9
- 238000000889 atomisation Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 abstract 2
- 238000010276 construction Methods 0.000 abstract 1
- 239000011550 stock solution Substances 0.000 description 18
- 239000000243 solution Substances 0.000 description 9
- 239000002245 particle Substances 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000001694 spray drying Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D3/00—Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials
- B05D3/04—Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials by exposure to gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
- B05B7/02—Spray pistols; Apparatus for discharge
- B05B7/06—Spray pistols; Apparatus for discharge with at least one outlet orifice surrounding another approximately in the same plane
- B05B7/062—Spray pistols; Apparatus for discharge with at least one outlet orifice surrounding another approximately in the same plane with only one liquid outlet and at least one gas outlet
- B05B7/066—Spray pistols; Apparatus for discharge with at least one outlet orifice surrounding another approximately in the same plane with only one liquid outlet and at least one gas outlet with an inner liquid outlet surrounded by at least one annular gas outlet
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
- B05B7/02—Spray pistols; Apparatus for discharge
- B05B7/10—Spray pistols; Apparatus for discharge producing a swirling discharge
Abstract
Description
【発明の詳細な説明】
［産業上の利用分野］
本発明はスプレードライヤーの運転立上り時の低圧力噴
霧にも対応することかできるノズル装置とそのノズル装
置を備えたスプレードライヤー装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a nozzle device that can handle low-pressure spraying at the start of operation of a spray dryer, and a spray dryer device equipped with the nozzle device.
［従来の技術］
通常、スプレードライヤー装置においては、その運転立
上り時に、過熱による製品の焦げつき、後工程の熱的保
護のため、噴霧乾燥室内の温度を安定させる必要かある
。その目的のため、同一の圧力ノズルにより、水の噴霧
を行っている。[Prior Art] Normally, in a spray dryer, it is necessary to stabilize the temperature inside the spray drying chamber at the start of operation to prevent the product from burning due to overheating and to protect the product from heat in subsequent processes. For that purpose, water is sprayed by the same pressure nozzle.
このような水噴霧を行う場合、水噴霧量は原液中の水分
に相当する量とする必要がある。原液の水分量は一般に
３０〜８０％であり、従って水の噴霧量は同様に原液の
所定噴霧量の３０〜８０％となり、圧力ノズルの特性上
から圧力は液の粘度等にもよるがほぼ１０〜８０％に低
下する。このため、圧力ノズルの特性上、水滴は大粒子
となり乾燥し難くなるため、未乾燥のまま乾燥室内に付
着し、壁面か濡れることとなる。このとき、引続いて原
液を噴霧した場合には、乾燥した粉体かその部分に付着
し、固化してしまうこととなる。When such water spraying is performed, the amount of water sprayed needs to be equivalent to the water content in the stock solution. The moisture content of the stock solution is generally 30 to 80%, so the amount of water sprayed is similarly 30 to 80% of the specified spray amount of the stock solution.Due to the characteristics of the pressure nozzle, the pressure is approximately 30% to 80%, although it depends on the viscosity of the liquid It decreases to 10-80%. Therefore, due to the characteristics of the pressure nozzle, the water droplets become large particles and are difficult to dry, so they adhere to the interior of the drying chamber undried, and the walls become wet. At this time, if the stock solution is subsequently sprayed, the dried powder will adhere to that area and solidify.
そこで、従来においては、第６図および第７図に示すよ
うな工夫がなされている。Therefore, in the past, measures have been taken as shown in FIGS. 6 and 7.
第６図は複数ノズルを設置した場合の例てあり、噴霧乾
燥室内の北部に複数のノズル１０を設け、水噴霧な行う
場合、ＩＩａ”Ｒノズル１０の本数を制御することによ
って低圧力噴霧を回避しているものである。Figure 6 shows an example of a case where multiple nozzles are installed. When multiple nozzles 10 are installed in the northern part of the spray drying chamber to perform water spraying, low pressure spraying can be achieved by controlling the number of IIa"R nozzles 10. It is something that is being avoided.
一方、第７図は水噴霧用ノズル１１を原液噴霧ノズル１
２とは別に設けた例を示している。On the other hand, in FIG. 7, the water spray nozzle 11 is replaced with the stock solution spray nozzle 1.
An example provided separately from 2 is shown.
［発明が解決しようとする課題］
しかしなから、第６図に示すものにおいては、ノズル間
隔を広くとる必要かあることと未噴霧ノズルかあるため
、液滴が均一に広がらず、温度のバラツキか生しる。ま
た、水の未噴霧ノズルに詰まりが生じるという問題があ
る。[Problem to be solved by the invention] However, in the case shown in Fig. 6, the nozzle spacing must be wide and there are some nozzles that are not spraying, so the droplets do not spread uniformly and the temperature varies. It will come to life. Further, there is a problem in that the nozzles that are not sprayed with water become clogged.
一方、第７図に示すものにおいては、水による原液噴霧
ノズルの冷却と洗浄かてきないため、原液噴霧ノズルで
原液の詰まりか生じるという問題かある。On the other hand, in the case shown in FIG. 7, since the undiluted solution spray nozzle cannot be cooled and cleaned with water, there is a problem that the undiluted solution spray nozzle is clogged with the undiluted solution.
本発明は、従来の技術の有するこのような問題点に鑑み
てなされたものであり、その目的とするところは、水を
低圧力噴霧する場合であっても、水滴が微粒化されて完
全に乾燥され、さらに噴霧ノズルの冷却か行われて原液
の詰まりか防止できるノズル装置とそれを備えたスプレ
ードライヤー装置を提供しようとするものである。The present invention has been made in view of the above-mentioned problems of the conventional technology, and its purpose is to atomize water droplets and completely eliminate them even when water is sprayed at low pressure. The object of the present invention is to provide a nozzle device that can be dried and further cooled to prevent clogging of the undiluted solution, and a spray dryer device equipped with the nozzle device.
［課題を解決するための手段］
−Ｆ記目的を達成するために、本発明は、原液吹出しの
ための圧力ノズルと、該圧力ノズルの周りに設けた高速
ガス吹出し用筒状体とからなるノズル装置δてあって、
該ノズル装置の先端部を先細り構造としたことを特徴と
するノズル装置、および、そのノズル装置を備えたスプ
レードライヤー装置である。[Means for Solving the Problems] - In order to achieve the object described in F, the present invention comprises a pressure nozzle for blowing out a stock solution, and a cylindrical body for high-speed gas blowing provided around the pressure nozzle. There is a nozzle device δ,
The present invention provides a nozzle device characterized in that the tip of the nozzle device has a tapered structure, and a spray dryer device equipped with the nozzle device.
また、このノズル装置として、原液吹出し先端部におけ
る圧力ノズルと高速ガス吹出し用筒状体の間に、高速ガ
スに旋回流を付与するためのスリットを形成すると、液
滴噴霧角度かさらに大きくなるため好ましい。In addition, in this nozzle device, if a slit is formed between the pressure nozzle at the tip of the raw solution blowout and the high-speed gas blowing cylindrical body to impart a swirling flow to the high-speed gas, the droplet spray angle will become even larger. preferable.
［作用］
圧力ノズルの周囲を高速ガス吹出し用の筒状体にて包囲
し、そこからガスを高速で吹出すため、圧力ノズルから
の噴霧か低圧力ての噴霧となる場合てあっても、水滴か
大粒子とならず、微粒化する。従って、水滴か未乾燥の
まま噴霧乾燥室内に付着することなく、完全に乾燥する
。[Function] The pressure nozzle is surrounded by a cylindrical body for blowing out gas at high speed, and gas is blown out from there at high speed, so even if the spray is from the pressure nozzle or at low pressure, It does not become water droplets or large particles, but becomes atomized. Therefore, the spray drying chamber is completely dried without any water droplets remaining undried.
［実施例］
以下、本発明を図示の実施例に基すいて更に詳細に説明
するが、本発明かこれらの実施例に限定されないことは
明らかであろう。[Examples] The present invention will be described in more detail below based on illustrated embodiments, but it will be clear that the present invention is not limited to these embodiments.
第１図は本発明のノズル装置の一実施例を示す説明図で
あり、第２図は第１図のノズル装置の先端部を示す部分
断面図である。FIG. 1 is an explanatory view showing one embodiment of the nozzle device of the present invention, and FIG. 2 is a partial sectional view showing the tip of the nozzle device of FIG. 1.
図において、ｌは原液（又は水）ポンプ、２はルーツブ
ロワ−１３はジャケットパイプ、４はエアーノズル、５
は原液（又は水）パイプ、６は原液（又は水）吹出し用
圧力ノズルを夫々示している。即ち、原液または水の吹
出しのための原液パイプ５の周りにジャケットパイプ３
を設け、その吹出し先端部である圧力ノズル６とエアー
ノズル４か第１図及び第２図に示すように、先端にいく
に従って径か小さくなる、いわゆる先細り構造を有して
いる。In the figure, l is the raw solution (or water) pump, 2 is the Roots blower, 13 is the jacket pipe, 4 is the air nozzle, and 5 is the
6 indicates a stock solution (or water) pipe, and 6 indicates a pressure nozzle for blowing out the stock solution (or water). That is, a jacket pipe 3 is installed around the stock solution pipe 5 for blowing out the stock solution or water.
As shown in FIGS. 1 and 2, the pressure nozzle 6 and air nozzle 4, which are the blowing tips thereof, have a so-called tapered structure in which the diameter becomes smaller toward the tip.
また、吹出し空気に旋回流を付与するため、第３図（ａ
）（ｂ）（ｃ）（ここで、（ａ）はモ面図、（ｂ）は底
面図、（ｃ）は側面図）、及び第４図に示す如く、圧力
ノズル６とエアーノズル４の間、あるいは圧力ノズル６
の外側部にスリッＩ〜７を設けることは、原液または木
の噴霧角か広がることから好ましい。In addition, in order to impart a swirling flow to the blown air,
) (b) (c) (where (a) is a top view, (b) is a bottom view, and (c) is a side view), and as shown in FIG. 4, the pressure nozzle 6 and the air nozzle 4 are or pressure nozzle 6
It is preferable to provide the slits I to 7 on the outer side of the container because the spray angle of the raw solution or wood will be widened.
ここで、圧力ノズル６における原液または水の１’ｆｌ
’Ａ正圧力、次に示す圧力ノズルの流出特性を表わす
一般式Ｉ、および使用する圧力ノズル（この場合はスブ
レイング社、ＳＸノズル）の液滴径に関する式■に従っ
て、適宜決定される。Here, 1'fl of the stock solution or water in the pressure nozzle 6
'A positive pressure is appropriately determined according to the following general formula I expressing the outflow characteristics of the pressure nozzle, and formula (2) regarding the droplet diameter of the pressure nozzle used (in this case, the SX nozzle manufactured by Sbreing).
Ｗ（ｋｇ／ｈ）＝に１・Ｄ２（ＩＩｌｌ）・Ｐｏ５（ｋ
ｇ／ｃ１１２）（Ｗ：処理量、Ｋ１ ：係数、Ｄニオリ
フイス径。W (kg/h) = 1・D2(IIll)・Po5(k
g/c112) (W: throughput, K1: coefficient, D niorifice diameter.
Ｐ・圧力）
・・・・・・よ
り ｐ（ｇｍ）＝ Ｋ２・Ｗ−’ ” （ｋｇ／Ｉｔ）
・μｏ”（ｃｐ）・Ｄ′、 ’、２（１１ｍ）
（Ｗ：処理量、ＤＰ ：液滴径、Ｋ２ ：係数、ＪＬ：
液粘度）
・・・・・・■
また、圧力ノズル６の周りに設けられるエアーノズル４
においては、空気の吹出し速度は８０ｍ／Ｓ以上、好ま
しくは１００ ｍ／ｓ以上であり、空気圧は一般に０
、 １ ｋｇ／ｃｓ２以上、好ましくは０．２ｋｇ／ａ
ｍ２以上で用いられるが、これに限られるものではなく
、ノズル構造の如何により上記数値範囲外で用いてもよ
い。P・Pressure) ...... From p (gm) = K2・W-' ” (kg/It)
・μo”(cp)・D′,′,2(11m) (W: Processing amount, DP: Droplet diameter, K2: Coefficient, JL:
liquid viscosity) ・・・・・・■ Also, the air nozzle 4 provided around the pressure nozzle 6
In this case, the air blowing speed is 80 m/s or more, preferably 100 m/s or more, and the air pressure is generally 0.
, 1 kg/cs2 or more, preferably 0.2 kg/a
m2 or more, but is not limited to this, and may be used outside the above numerical range depending on the nozzle structure.
次に、本発明のノズル装とを組込んだスプレードライヤ
ー装置の一例を示す第５図に基いて、スプレードライヤ
ー装置の操作を説明する。Next, the operation of the spray dryer device will be explained based on FIG. 5, which shows an example of a spray dryer device incorporating the nozzle arrangement of the present invention.
まず、運転立上り時において、原液ポンプｌにより木を
原液パイプ５を介して圧力ノズル６により水噴霧を行な
う。この場合、相当な低圧力噴霧となるか、圧力ノズル
６の周りから空気か高速て吹出され、また、好ましくは
スリット７により吹出し空気に旋回流か付与される。そ
うすると、圧力ノズル６から吹き出される水滴か所望の
液滴径まて微粒化されるのである。First, at the start of operation, water is sprayed onto the wood by the stock solution pump 1 through the stock solution pipe 5 and the pressure nozzle 6. In this case, either the air is sprayed at a considerably low pressure or the air is blown out from around the pressure nozzle 6 at high speed, and preferably the slit 7 imparts a swirling flow to the blown air. Then, the water droplets blown out from the pressure nozzle 6 are atomized to the desired droplet diameter.
このように水滴が所望径まて微粒化されると、スプレー
ドライヤー装置の乾燥室８内に吹き込まれる熱風Ａによ
って水滴が完全に乾煙されることとなる。そうすると、
乾燥室８には未乾燥水分が残存することなく、乾燥室８
内における温度分布が殆どなくなり、即ち、乾燥室８内
における温度を一定とすることができる。When the water droplets are atomized to a desired diameter in this manner, the water droplets are completely dried and smoked by the hot air A blown into the drying chamber 8 of the spray dryer. Then,
The drying chamber 8 is completely dry without any undried moisture remaining in the drying chamber 8.
There is almost no temperature distribution within the drying chamber 8, that is, the temperature within the drying chamber 8 can be kept constant.
次いで、スプレードライヤー装置の乾燥室８内には、所
定目的に対応する原液が上記ノズル装置の圧力ノズル６
を経て吹き込まれ、所定の粉体製品か得られることとな
る。Next, in the drying chamber 8 of the spray dryer device, a stock solution corresponding to a predetermined purpose is supplied to the pressure nozzle 6 of the nozzle device.
The powder is blown through the process to obtain the desired powder product.
尚、このノズル装置により原液を噴霧する場合において
、圧力ノズル６の周りに少量の空気をエアーノズル４を
介して流すことは、ノズル装置を冷却して原液の詰まり
を防止できることから好ましいことである。In addition, when spraying the stock solution using this nozzle device, it is preferable to flow a small amount of air around the pressure nozzle 6 through the air nozzle 4, since this can cool the nozzle device and prevent clogging of the stock solution. .
次に、本発明装置による微粒化について、更に具体的な
実施結果を説明する。Next, more specific implementation results regarding atomization using the apparatus of the present invention will be described.
（実施例１）
表−１に示す条件にて原液及び水の微粒化試験を行なっ
た。尚、圧力ノズル６は断面六角形のスプレインク社
ＳＸノズルを使用し、その周囲を断面円形の筒状体で覆
ってエアーノズル４とした。Ｓｘノズルと筒状体の間隔
は広い箇所で約５■、狭い箇所で約３■であり、筒状体
の先端部の孔径は７ｍｍ（φ）であった。(Example 1) An atomization test of stock solution and water was conducted under the conditions shown in Table-1. The pressure nozzle 6 is made by Spray Ink and has a hexagonal cross section.
An air nozzle 4 was prepared by using an SX nozzle and covering its periphery with a cylindrical body having a circular cross section. The distance between the Sx nozzle and the cylindrical body was about 5 cm at the widest point and about 3 cm at the narrowest point, and the hole diameter at the tip of the cylindrical body was 7 mm (φ).
結果を表−１に示す。The results are shown in Table-1.
（以下、余白）
表−１
圧力ノズルはスプレインク社 Ｓｘノズルを使用また、
本発明のノズル装りにおいて、高速空気に旋回流を付が
した場合には、次の通りの結果となった。(The following is a blank space) Table-1 The pressure nozzle is a Spray Ink Sx nozzle.
In the nozzle arrangement of the present invention, when swirling flow was applied to high-speed air, the following results were obtained.
（実施例２）
次に、実施例１におけるノズルを使用し、大粒径の粒子
を得るため、ノズルオリフィス径を変更し、大形の乾燥
室を用いて試験を行った。その結果を表−２に示す。(Example 2) Next, a test was conducted using the nozzle in Example 1, changing the nozzle orifice diameter and using a large drying chamber in order to obtain large particles. The results are shown in Table-2.
（以下、余白）
表−２
以北の結果から明らかな通り、従来ノズルに比し本発明
ノズルによれば、充分に水滴が微粒化されることかわか
る。また、吹出し空気に旋回流を付ｌｊ、 シた場合に
は噴霧角か広がるので乾燥性も向上することになる。(The following is a blank space) As is clear from the results shown in Table 2, it can be seen that water droplets are sufficiently atomized with the nozzle of the present invention compared to the conventional nozzle. Furthermore, when a swirling flow is applied to the blown air, the spray angle becomes wider, which improves drying performance.
［発明の効果］
以１；説明したように、本発明のノズル装置によれば、
水を低圧力噴霧する場合であっても、水滴か微粒化され
て完全に乾燥され、さらに噴霧ノズルの冷却か行われて
原液の詰まりか防止できる。[Effects of the Invention] 1. As explained above, according to the nozzle device of the present invention,
Even when water is sprayed at low pressure, water droplets are atomized and completely dried, and the spray nozzle is cooled to prevent clogging of the raw solution.
従って、このノズル装置を組込んだスプレードライヤー
装置においては、水を低圧力噴霧した後の原液の噴霧な
効果的且つ安定して行なうことかできる。Therefore, in a spray dryer device incorporating this nozzle device, it is possible to effectively and stably spray water after low-pressure spraying and then spray the stock solution.
第１図は本発明のノズル装置の一実施例を示す説明図、
第２図は第１図のノズル装置の先端部を示す部分断面図
、第３図（ａ）（ｂ）（ｃ）はノズル装置におけるスリ
ット形状の一例を示すものて、（ａ）は上面図、（ｂ）
は底面図、（ｃ）は側面図である。第４図はノズル装置
におけるスリット形状の他の例を示す底面図、第５図は
本発明のノズル装置を組込んだスプレードライヤー装置
の一例を示す概略図、第６図及び第７図はともに従来の
ノズル装置を示す説明図である。
ｌ・・・原液ポンプ、２・・・ルーツブロワ−１３・・
・ジャケットパイプ、４・・・エアーノズル、５・・・
原液バイブ、６・・・圧力ノズル、７・・・スリット、
８・・・乾燥室。FIG. 1 is an explanatory diagram showing an embodiment of the nozzle device of the present invention,
Fig. 2 is a partial sectional view showing the tip of the nozzle device in Fig. 1, Fig. 3 (a), (b), and (c) show examples of slit shapes in the nozzle device, and (a) is a top view. ,(b)
is a bottom view, and (c) is a side view. FIG. 4 is a bottom view showing another example of the slit shape in the nozzle device, FIG. 5 is a schematic diagram showing an example of a spray dryer device incorporating the nozzle device of the present invention, and FIGS. 6 and 7 are both It is an explanatory view showing a conventional nozzle device. l...Stock pump, 2...Roots blower 13...
・Jacket pipe, 4...Air nozzle, 5...
Raw solution vibrator, 6...pressure nozzle, 7...slit,
8...Drying room.
Claims (3)
の周りに設けた高速ガス吹出し用筒状体とからなるノズ
ル装置であって、該ノズル装置の先端部を先細り構造と
したことを特徴とするノズル装置。(1) A nozzle device consisting of a pressure nozzle for blowing out raw liquid and a cylindrical body for blowing out high-speed gas provided around the pressure nozzle, characterized in that the tip of the nozzle device has a tapered structure. Nozzle device.
ス吹出し用筒状体の間に、高速ガスに旋回流を付与する
ためのスリットを形成した特許請求の範囲第１項記載の
ノズル装置。(2) The nozzle device according to claim 1, wherein a slit for imparting a swirling flow to the high-speed gas is formed between the pressure nozzle and the high-speed gas blowing cylindrical body at the tip of the nozzle device.
の周りに設けた高速ガス吹出し用筒状体とからなり、そ
の先端部を先細り構造としたノズル装置を乾燥室の上部
に備えるとともに、該乾燥室内への熱風吹込み口及び該
乾燥室からの排気口を備えたことを特徴とするスプレー
ドライヤー装置。(3) A nozzle device consisting of a pressure nozzle for blowing out the raw solution and a cylindrical body for blowing out high-speed gas provided around the pressure nozzle, the tip of which is tapered, is provided in the upper part of the drying chamber; A spray dryer device comprising a hot air blowing port into the drying chamber and an exhaust port from the drying chamber.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63019008A JP2524379B2 (en) | 1988-01-29 | 1988-01-29 | Nozzle device and spray dryer device incorporating it |
| EP19890113481 EP0408801B1 (en) | 1988-01-29 | 1989-07-21 | Spray drying apparatus |
| US07/563,142 US5227017A (en) | 1988-01-29 | 1990-08-06 | Spray drying apparatus equipped with a spray nozzle unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63019008A JP2524379B2 (en) | 1988-01-29 | 1988-01-29 | Nozzle device and spray dryer device incorporating it |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01194901A true JPH01194901A (en) | 1989-08-04 |
| JP2524379B2 JP2524379B2 (en) | 1996-08-14 |
Family
ID=11987480
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63019008A Expired - Lifetime JP2524379B2 (en) | 1988-01-29 | 1988-01-29 | Nozzle device and spray dryer device incorporating it |
Country Status (2)
| Country | Link |
|---|---|
| EP (1) | EP0408801B1 (en) |
| JP (1) | JP2524379B2 (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0408801A1 (en) * | 1988-01-29 | 1991-01-23 | Ohkawara Kakohki Co., Ltd. | Spray drying apparatus |
| US5499768A (en) * | 1989-05-31 | 1996-03-19 | Ohkawara Kakohki Co., Ltd. | Spray nozzle unit |
| JP2013013891A (en) * | 2011-07-01 | 2013-01-24 | Lechler Gmbh | Solid conical injection nozzle |
| JP2017529234A (en) * | 2014-07-04 | 2017-10-05 | サントル ナスィオナル ド ラ ルシェルシュ スィアンティフィク（セ．エン．エル．エス．） | Method for producing co-crystals by flash evaporation |
| US9808424B2 (en) | 2010-04-09 | 2017-11-07 | Pacira Pharmaceuticals, Inc. | Method for formulating large diameter synthetic membrane vesicles |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6051256A (en) | 1994-03-07 | 2000-04-18 | Inhale Therapeutic Systems | Dispersible macromolecule compositions and methods for their preparation and use |
| US20030203036A1 (en) | 2000-03-17 | 2003-10-30 | Gordon Marc S. | Systems and processes for spray drying hydrophobic drugs with hydrophilic excipients |
| US7575761B2 (en) | 2000-06-30 | 2009-08-18 | Novartis Pharma Ag | Spray drying process control of drying kinetics |
| DE60227691D1 (en) | 2001-11-01 | 2008-08-28 | Nektar Therapeutics | SPRAY DRYING PROCESS |
| GB0216562D0 (en) | 2002-04-25 | 2002-08-28 | Bradford Particle Design Ltd | Particulate materials |
| US9339459B2 (en) | 2003-04-24 | 2016-05-17 | Nektar Therapeutics | Particulate materials |
| CA2508870C (en) | 2002-12-30 | 2012-10-16 | Nektar Therapeutics | Prefilming atomizer |
| US10569187B2 (en) | 2011-02-28 | 2020-02-25 | Gea Process Engineering A/S | External mixing pressurized two-fluid nozzle and a spray drying method |
| EP2680978B1 (en) | 2011-02-28 | 2021-07-21 | GEA Process Engineering A/S | Spray drying apparatus comprising an external mixing pressurized two-fluid nozzle and a spray drying method |
| DE102011120717A1 (en) * | 2011-12-12 | 2013-06-13 | Sm-Klebetechnik Vertriebs Gmbh | Fluid nozzle for application of highly viscous materials e.g. high viscosity adhesive, has deflector metal sheet such as lock washer provided in gas outlet which is arranged around substance outlet |
| US20240123367A1 (en) * | 2022-09-15 | 2024-04-18 | Velico Medical, Inc. | Nozzle For A Disposable For Use With Spray Drying System |
| WO2024059771A1 (en) * | 2022-09-15 | 2024-03-21 | Velico Medical, Inc. | Two-phase delivery of plasma |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE476795A (en) * | 1946-12-31 | 1947-10-17 | ||
| JPS5141693B1 (en) * | 1971-05-24 | 1976-11-11 | ||
| JPS6110775Y2 (en) * | 1979-10-25 | 1986-04-05 | ||
| JP2524379B2 (en) * | 1988-01-29 | 1996-08-14 | 大川原化工機株式会社 | Nozzle device and spray dryer device incorporating it |
-
1988
- 1988-01-29 JP JP63019008A patent/JP2524379B2/en not_active Expired - Lifetime
-
1989
- 1989-07-21 EP EP19890113481 patent/EP0408801B1/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0408801A1 (en) * | 1988-01-29 | 1991-01-23 | Ohkawara Kakohki Co., Ltd. | Spray drying apparatus |
| US5499768A (en) * | 1989-05-31 | 1996-03-19 | Ohkawara Kakohki Co., Ltd. | Spray nozzle unit |
| US9808424B2 (en) | 2010-04-09 | 2017-11-07 | Pacira Pharmaceuticals, Inc. | Method for formulating large diameter synthetic membrane vesicles |
| US10045941B2 (en) | 2010-04-09 | 2018-08-14 | Pacira Pharmaceuticals, Inc. | Method for formulating large diameter synthetic membrane vesicles |
| JP2013013891A (en) * | 2011-07-01 | 2013-01-24 | Lechler Gmbh | Solid conical injection nozzle |
| US9216426B2 (en) | 2011-07-01 | 2015-12-22 | Lechler Gmbh | Solid cone nozzle |
| JP2017529234A (en) * | 2014-07-04 | 2017-10-05 | サントル ナスィオナル ド ラ ルシェルシュ スィアンティフィク（セ．エン．エル．エス．） | Method for producing co-crystals by flash evaporation |
| JP2020108890A (en) * | 2014-07-04 | 2020-07-16 | サントル ナショナル ドゥ ラ ルシェルシュ シアンティフィック | Method for producing cocrystals by means of flash evaporation |
Also Published As
| Publication number | Publication date |
|---|---|
| EP0408801A1 (en) | 1991-01-23 |
| EP0408801B1 (en) | 1995-11-15 |
| JP2524379B2 (en) | 1996-08-14 |
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