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1. 发明公开

CN106914158A 一种固体溶质加速溶解装置无效
公开(公告)号：CN106914158A
公开(公告)日：2017-07-04
申请号：CN201510984034.3
申请日：2015-12-24
申请人：浙江金马实业有限公司
发明人：屠旭峰
IPC分类号： B01F1/00 , B01F9/00 , B01F9/10 , B01F11/02 , B01F13/10
CPC分类号： B01F1/00 , B01F1/0022 , B01F1/0038 , B01F9/0005 , B01F9/10 , B01F11/0266 , B01F11/0283 , B01F13/1025 , B01F2001/0072 , B01F2009/0061
摘要：本发明涉及固体溶质溶解技术领域，公开了一种固体溶质加速溶解装置，包括壳体、设在壳体上端的盖板，盖板的一侧与壳体开口端侧面铰接，盖板的另一侧与壳体的另一侧卡接；壳体底部设有超声波发生器，超声波发生器的上方设有换能器，换能器的上方设有水平的支撑板，支撑板的下侧面通过若干支撑杆与壳体底面连接，支撑板的上侧面设有托盘，壳体的外侧设有控制面板，控制面板上设有超声波调节旋钮、频率显示器。本发明具有能促进溶质快速溶解的有益效果。

2. 发明授权

CN106029216B 微粒的制造方法失效
公开(公告)号：CN106029216B
公开(公告)日：2018-05-08
申请号：CN201580009158.8
申请日：2015-02-18
申请人： M技术株式会社
发明人：榎村真一
IPC分类号： B01J19/00 , C09B48/00 , C09B67/14 , C09B67/20 , A61K31/405
CPC分类号： B01F1/0011 , A61K31/405 , B01F3/0807 , B01F7/00775 , B01F7/164 , B01F7/166 , B01F7/1675 , B01F7/247 , B01F15/00175 , B01F15/00376 , B01F2001/0072 , B01F2215/005 , B01J4/002 , B01J19/0066 , B01J19/18 , B01J19/1887 , B01J2219/00772 , B01J2219/00779 , C09B67/0036 , C09B67/009 , C09B67/0095 , C09B67/0097
摘要：提供微粒的制造方法，其具有：使用具有进行旋转的搅拌叶片的搅拌机而使至少1种的微粒原料在溶剂中溶解来得到微粒原料溶液的溶解步骤；和将用于从微粒原料溶液使微粒原料析出的至少1种的析出溶剂、和微粒原料溶液导入对向配设的、可接近和/或分离的、至少一方相对于另一方相对地进行旋转的至少2个处理用面间、在至少2个处理用面间形成的薄膜流体中混合而使微粒析出的析出步骤。在上述溶解步骤中，对于由采用搅拌机的搅拌时间条件、搅拌叶片的周向速度条件、微粒原料溶液的温度条件所规定的搅拌能量，通过使上述条件中的至少1个变化而使其增减，通过搅拌能量的增减，控制析出步骤中得到的微粒的结晶度、晶型。

3. 发明公开

CN107866157A 一种气体搅拌设备无效
公开(公告)号：CN107866157A
公开(公告)日：2018-04-03
申请号：CN201711316064.2
申请日：2017-12-12
申请人：四川新驱科为科技有限公司
发明人：王前明
IPC分类号： B01F1/00 , B01F13/02
CPC分类号： B01F1/0022 , B01F13/0283 , B01F2001/0072
摘要：本发明公开了一种气体搅拌设备，包括罐体，设置在管体上端的入料口和排气管，设置在罐体内壁上的杂质收集管，环绕在管体内壁上且位于杂质收集管下方的支撑圈，固定在支撑圈上的防护网，设置在罐体下侧的过气腔，贯穿罐体且将罐体与过气腔相连接的进气结构。本发明提供一种气体搅拌设备，提供了一种新的搅拌机设计思路，降低了搅拌机内部的清理难度，摒除了搅拌棒，进一步降低了搅拌机的内部结构。

4. 发明公开

CN107866156A 一种自除杂无搅拌棒式搅拌机无效
公开(公告)号：CN107866156A
公开(公告)日：2018-04-03
申请号：CN201711315296.6
申请日：2017-12-12
申请人：四川新驱科为科技有限公司
发明人：王前明
IPC分类号： B01F1/00 , B01F13/02 , B01F15/00
CPC分类号： B01F1/0022 , B01F13/0283 , B01F15/00993 , B01F2001/0072
摘要：本发明公开了一种自除杂无搅拌棒式搅拌机，包括罐体，设置在管体上端的入料口和排气结构，设置在罐体内壁上的杂质收集管，环绕在管体内壁上且位于杂质收集管下方的支撑圈，固定在支撑圈上的防护网，设置在罐体下侧的过气腔，贯穿罐体且将罐体与过气腔相连接的进气口，以及设置在防护网下侧的旋转扇。本发明提供一种自除杂无搅拌棒式搅拌机，提供了一种新的搅拌机设计思路，降低了搅拌机内部的清理难度，摒除了搅拌棒，进一步降低了搅拌机的内部结构。

5. 发明公开

CN106029216A 微粒的制造方法失效
公开(公告)号：CN106029216A
公开(公告)日：2016-10-12
申请号：CN201580009158.8
申请日：2015-02-18
申请人： M技术株式会社
发明人：榎村真一
IPC分类号： B01J19/00 , C09B48/00 , C09B67/14 , C09B67/20 , A61K31/405
CPC分类号： B01F1/0011 , A61K31/405 , B01F3/0807 , B01F7/00775 , B01F7/164 , B01F7/166 , B01F7/1675 , B01F7/247 , B01F15/00175 , B01F15/00376 , B01F2001/0072 , B01F2215/005 , B01J4/002 , B01J19/0066 , B01J19/18 , B01J19/1887 , B01J2219/00772 , B01J2219/00779 , C09B67/0036 , C09B67/009 , C09B67/0095 , C09B67/0097
摘要：提供微粒的制造方法，其具有：使用具有进行旋转的搅拌叶片的搅拌机而使至少1种的微粒原料在溶剂中溶解来得到微粒原料溶液的溶解步骤；和将用于从微粒原料溶液使微粒原料析出的至少1种的析出溶剂、和微粒原料溶液导入对向配设的、可接近和/或分离的、至少一方相对于另一方相对地进行旋转的至少2个处理用面间、在至少2个处理用面间形成的薄膜流体中混合而使微粒析出的析出步骤。在上述溶解步骤中，对于由采用搅拌机的搅拌时间条件、搅拌叶片的周向速度条件、微粒原料溶液的温度条件所规定的搅拌能量，通过使上述条件中的至少1个变化而使其增减，通过搅拌能量的增减，控制析出步骤中得到的微粒的结晶度、晶型。

6. 发明公开

CN105435662A 一种灌溉用肥料融化装置无效
公开(公告)号：CN105435662A
公开(公告)日：2016-03-30
申请号：CN201510986373.5
申请日：2015-12-25
申请人：重庆旭鹏生态农业开发有限公司
发明人：郑继砚
IPC分类号： B01F1/00 , B01F15/02
CPC分类号： B01F1/0022 , B01F1/0033 , B01F1/0038 , B01F15/0203 , B01F15/0216 , B01F2001/0072 , B01F2001/0088 , B01F2001/0094 , B01F2215/0054
摘要：本发明公开了一种灌溉用肥料融化装置，涉及一种农业生产装置；灌溉用肥料融化装置包括溶解池、位于溶解池下方的液态肥料的收集器以及供水系统，溶解池与收集器之间设置一具有若干漏水孔的隔板，隔板上铺设有一层过滤膜；过滤膜上堆积有肥料颗粒，在收集器内设置有一用于监测液态肥料浓度的电导电极和用于调节浓度的变频泵，收集器的下部设置有一输出管，在输出管上连接有一水泵；供水系统包括进水干管，进水干管的出水端连接有一进水阀和增压泵，且进水干管上连接有若干间隔排列的出水管，每一出水管上间隔设置有若干喷头，且喷头从收集器伸入到溶解池中。本装置可以加快肥料的溶解速率，同时还能保证浇灌效率。

7. 发明申请

US20150217241A1 DISPENSERS 审中-公开
标题翻译：分配者
公开(公告)号：US20150217241A1
公开(公告)日：2015-08-06
申请号：US14424690
申请日：2013-09-02
申请人： BUZZ TRADING 197 (PROPRIETARY) LIMITED
发明人： Peter James Buchan
IPC分类号： B01F1/00 , C02F1/68 , C02F1/50
CPC分类号： B01F1/0027 , B01F2001/0055 , B01F2001/0072 , C02F1/50 , C02F1/68 , C02F2305/00 , Y10T137/4891
摘要： The invention provides a dispenser to dispense, in operation, particulate, soluble chemical agent, by dissolution, from a compacted or compressed harm thereof, into liquid that flows along a flow path. The dispenser comprises a body defining a liquid treatment chamber, an inlet to the liquid treatment chamber, through which inlet feed liquid can, in operation, continuously be ted into the treatment chamber, and an outlet from the treatment chamber, through which outlet product liquid, containing dissolved chemical agent can, in operation, continuously leave the treatment chamber. The dispenser is configured such that a chemical agent artefact comprising the particulate, soluble chemical agent in a compacted or compressed form is arrangeable in the dispenser, in use in a predetermined position in which the artefact is exposed to or accessible from inside of the treatment chamber only along a liquid contact surface provided by part of an outer surface thereof, which part extends along an artefact access plane defined in the dispenser in use at the predetermined position, such that liquid which is fed to the treatment chamber through the inlet, in operation, can contact the artefact only along the liquid contact surface and necessarily by passing across the artefact access plane.
摘要翻译：本发明提供了一种分配器，其在操作中将颗粒状可溶化学试剂通过从其压实或压缩的危害中溶解成沿着流动路径流动的液体。分配器包括限定液体处理室的主体，液体处理室的入口，入口进料液体可以在其中连续进入处理室，以及来自处理室的出口，出口产物液体，含有溶解的化学药剂，可在运行中连续离开处理室。分配器构造成使得包含颗粒状可溶性化学试剂的化学试剂人造物在压实或压缩形式中可布置在分配器中，在预定位置中，其中人造物暴露于处理室内部或从处理室内部仅沿着由其外表面的一部分提供的液体接触表面，该部分沿着在预定位置处使用中限定在分配器中的假象存取平面延伸，使得在操作中通过入口被供给到处理室的液体，只能沿着液体接触表面接触人造物，并且必须通过穿过伪影访问平面。

8. 发明申请

US20170246595A1 METHOD FOR PRODUCING MICROPARTICLES 审中-公开
公开(公告)号：US20170246595A1
公开(公告)日：2017-08-31
申请号：US15119965
申请日：2015-02-18
申请人： M. TECHNIQUE CO., LTD.
发明人： Masakazu ENOMURA
IPC分类号： B01F1/00 , C09B67/42 , C09B67/22 , B01F7/24 , B01F15/00 , A61K31/405 , B01F7/16
CPC分类号： B01F1/0011 , A61K31/405 , B01F3/0807 , B01F7/00775 , B01F7/164 , B01F7/166 , B01F7/1675 , B01F7/247 , B01F15/00175 , B01F15/00376 , B01F2001/0072 , B01F2215/005 , B01J4/002 , B01J19/0066 , B01J19/18 , B01J19/1887 , B01J2219/00772 , B01J2219/00779 , C09B67/0036 , C09B67/009 , C09B67/0095 , C09B67/0097
摘要： This fine particle production method involves a dissolving step in which a stirrer having a rotating stirring blade is used to dissolve at least one type of fine particle raw material in a solvent to obtain a fine particle raw material solution, and a precipitation step in which the fine particle raw material solution and at least one type of precipitation solvent for precipitating the fine particle raw material from the fine particle raw material solution are introduced between at least two treatment surfaces which are arranged oppositely one another, can move closer to and farther apart from one another, and at least one of which can rotate relative to the other, and the fine particle raw material solution and the at least one type of precipitation solvent are mixed in a thin film fluid formed between the at least two treatment surfaces, and the fine particles are precipitated. The stirring energy is determined by the stirring time conditions of the stirrer, the circumferential velocity conditions of the stirring blade, and the temperature conditions of the fine particle raw material solution, and in the dissolving step, the stirring energy is varied by changing at least one of the aforementioned conditions, and by changing the stirring energy, the degree of crystallization and the crystal form of the fine particles obtained in the precipitation step are controlled.

9. 发明公开

EP3112017A1 FINE PARTICLE PRODUCTION METHOD 审中-公开
标题翻译： FEINPARTIKELHERSTELLUNGSVERFAHREN
公开(公告)号：EP3112017A1
公开(公告)日：2017-01-04
申请号：EP15752000.8
申请日：2015-02-18
申请人： M Technique Co., Ltd.
发明人： ENOMURA Masakazu
IPC分类号： B01J19/00 , C09B48/00 , C09B67/14 , C09B67/20 , A61K31/405
CPC分类号： B01F1/0011 , A61K31/405 , B01F3/0807 , B01F7/00775 , B01F7/164 , B01F7/166 , B01F7/1675 , B01F7/247 , B01F15/00175 , B01F15/00376 , B01F2001/0072 , B01F2215/005 , B01J4/002 , B01J19/0066 , B01J19/18 , B01J19/1887 , B01J2219/00772 , B01J2219/00779 , C09B67/0036 , C09B67/009 , C09B67/0095 , C09B67/0097
摘要： This fine particle production method involves a dissolving step in which a stirrer having a rotating stirring blade is used to dissolve at least one type of fine particle raw material in a solvent to obtain a fine particle raw material solution, and a precipitation step in which the fine particle raw material solution and at least one type of precipitation solvent for precipitating the fine particle raw material from the fine particle raw material solution are introduced between at least two treatment surfaces which are arranged oppositely one another, can move closer to and farther apart from one another, and at least one of which can rotate relative to the other, and the fine particle raw material solution and the at least one type of precipitation solvent are mixed in a thin film fluid formed between the at least two treatment surfaces, and the fine particles are precipitated. The stirring energy is determined by the stirring time conditions of the stirrer, the circumferential velocity conditions of the stirring blade, and the temperature conditions of the fine particle raw material solution, and in the dissolving step, the stirring energy is varied by changing at least one of the aforementioned conditions, and by changing the stirring energy, the degree of crystallization and the crystal form of the fine particles obtained in the precipitation step are controlled.
摘要翻译：这种微粒生产方法包括一种溶解步骤，其中使用具有旋转搅拌叶片的搅拌器将至少一种类型的细颗粒原料溶解在溶剂中以获得细颗粒原料溶液，并且沉淀步骤，其中微粒原料溶液和至少一种用于使细粒原料溶液中的微粒原料沉淀的沉淀溶剂引入到彼此相对布置的至少两个处理表面之间，可以更靠近并远离并且其中至少一个可以相对于另一个旋转，并且将细颗粒原料溶液和至少一种沉淀溶剂混合在形成在至少两个处理表面之间的薄膜流体中，并且细颗粒沉淀。通过搅拌器的搅拌时间条件，搅拌叶片的圆周速度条件和微粒原料溶液的温度条件来确定搅拌能量，并且在溶解步骤中，搅拌能量通过至少改变上述条件之一，并且通过改变在沉淀步骤中获得的微粒的搅拌能量，结晶度和晶体形状来控制。

10. 发明公开

EP3112017A4 FINE PARTICLE PRODUCTION METHOD 审中-公开
公开(公告)号：EP3112017A4
公开(公告)日：2018-01-03
申请号：EP15752000
申请日：2015-02-18
申请人： M TECHNIQUE CO LTD
发明人： ENOMURA MASAKAZU
IPC分类号： B01J19/00 , A61K31/405 , C09B48/00 , C09B67/14 , C09B67/20
CPC分类号： B01F1/0011 , A61K31/405 , B01F3/0807 , B01F7/00775 , B01F7/164 , B01F7/166 , B01F7/1675 , B01F7/247 , B01F15/00175 , B01F15/00376 , B01F2001/0072 , B01F2215/005 , B01J4/002 , B01J19/0066 , B01J19/18 , B01J19/1887 , B01J2219/00772 , B01J2219/00779 , C09B67/0036 , C09B67/009 , C09B67/0095 , C09B67/0097
摘要： This fine particle production method involves a dissolving step in which a stirrer having a rotating stirring blade is used to dissolve at least one type of fine particle raw material in a solvent to obtain a fine particle raw material solution, and a precipitation step in which the fine particle raw material solution and at least one type of precipitation solvent for precipitating the fine particle raw material from the fine particle raw material solution are introduced between at least two treatment surfaces which are arranged oppositely one another, can move closer to and farther apart from one another, and at least one of which can rotate relative to the other, and the fine particle raw material solution and the at least one type of precipitation solvent are mixed in a thin film fluid formed between the at least two treatment surfaces, and the fine particles are precipitated. The stirring energy is determined by the stirring time conditions of the stirrer, the circumferential velocity conditions of the stirring blade, and the temperature conditions of the fine particle raw material solution, and in the dissolving step, the stirring energy is varied by changing at least one of the aforementioned conditions, and by changing the stirring energy, the degree of crystallization and the crystal form of the fine particles obtained in the precipitation step are controlled.

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