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1. 发明专利

JP6065836B2 界面活性剤水溶液の濃縮回収方法有权
标题翻译：表面活性剂水溶液的浓度回收方法
公开(公告)号：JP6065836B2
公开(公告)日：2017-01-25
申请号：JP2013528997
申请日：2012-08-09
申请人：旭硝子株式会社
发明人：二川典史 , 永野重行
IPC分类号： B01D1/16
CPC分类号： B01D1/16 , B01D1/12 , B01D1/20 , B01D19/02 , B01D3/06 , C08F6/16 , C08F6/24 , C08J11/00 , C11D1/04

2. 发明专利

JPWO2013024790A1 界面活性剤水溶液の濃縮回収方法有权
标题翻译：表面活性剂水溶液的浓度回收方法
公开(公告)号：JPWO2013024790A1
公开(公告)日：2015-03-05
申请号：JP2013528997
申请日：2012-08-09
申请人：旭硝子株式会社
发明人：典史二川 , 典史二川 , 重行永野 , 重行永野
IPC分类号： B01D1/16
CPC分类号： B01D1/16 , B01D1/12 , B01D1/20 , B01D3/06 , B01D19/02 , B05B1/00 , B05B1/06 , B05B1/34 , C08F6/16 , C08F6/24 , C08J11/00 , C11D1/04 , C08L27/18
摘要：発泡を抑えつつ界面活性剤水溶液を蒸発濃縮し、界面活性剤を高濃度化した界面活性剤水溶液を高効率で簡便に得ることができる界面活性剤水溶液の濃縮回収方法の提供。ガス化可能な界面活性剤と水性溶媒を含有する界面活性剤水溶液を蒸発濃縮して、界面活性剤を高濃度化する界面活性剤水溶液の濃縮回収方法であって、蒸発缶12内に前記界面活性剤水溶液を収容し、蒸発缶12内の界面活性剤水溶液の温度を、蒸発缶12内の圧力下における前記水性溶媒の沸点より低い温度とし、前記界面活性剤水溶液の一部を蒸発缶12から抜き出し、過熱器14で界面活性剤と水性溶媒全体を環状流または環状噴霧流とする条件で過熱して、出口側が一旦狭くなった後に広がった形状のノズル32から蒸発缶12内に噴霧し、前記水性溶媒を蒸発させて除去する界面活性剤水溶液の濃縮回収方法。
摘要翻译：含水表面活性剂溶液被蒸发，同时抑制起泡，提供高度浓缩的浓缩表面活性剂水溶液可高效率地方便地获得表面活性剂水溶液的回收方法的洗涤剂。蒸发含有可气化的表面活性剂和水性溶剂的表面活性剂水溶液，表面活性剂的表面活性剂水溶液富集的浓度恢复的方法，该接口蒸发器12 含有活性剂溶液，该表面活性剂水溶液的在蒸发器12的温度，该温度比水性溶剂的压力蒸发器12的下方的沸点低，蒸发器12中的表面活性剂水溶液的一部分从，表面活性剂和总的水性溶剂过热器14和过热条件环形流或环形雾流从喇叭状的喷嘴32成为出口侧一旦窄蒸发器12后喷射的撤回中，表面活性剂水溶液的浓度恢复方法来通过蒸发除去所述水性溶剂。

3. 发明专利

JP2017516899A 脱去装置｛ＳＴＲＩＰＰＩＮＧＡＰＰＡＲＡＴＵＳ｝有权
公开(公告)号：JP2017516899A
公开(公告)日：2017-06-22
申请号：JP2016568846
申请日：2015-05-28
申请人：エルジー・ケム・リミテッド
发明人：ホ、チャン‐フェ , チュ、ウン‐チョン , シン、テ‐ヨン , シン、チュン‐ホ
IPC分类号： C08F6/10
CPC分类号： C08F6/003 , B01D1/12 , C08F6/00 , C08L27/06
摘要：本出願は、ポリビニルクロライド内の未反応ビニルクロライド単量体の除去方法に関するものであって、例示的な、本出願の脱去装置及び上記脱去装置及び方法によると、スチームを用いた脱去工程において、除去しようとする対象物質を含む原料とスチームととの間の温度差を最小化し、上記脱去工程で気泡の発生を抑制することができ、これにより、上記除去しようとする対象物質、特に、ポリビニルクロライド内の未反応ビニルクロライド単量体の除去効率を増加させることができ、上記脱去装置内で発生する気泡を除去するための洗浄周期を減少させることができ、工程の経済性が確保できるだけでなく、上記気泡を除去するための消泡剤を使用する場合に現れることがある、最終製品の品質低下を防止することができる。【選択図】図1

4. 发明专利

JP3718227B2 Desalination method and apparatus of seawater 失效
公开(公告)号：JP3718227B2
公开(公告)日：2005-11-24
申请号：JP50920296
申请日：1995-09-04
申请人：ホイス、ヤコブ
发明人：ホイス、ヤコブ
IPC分类号： B01D1/00 , B01D1/12 , B01D1/28 , B01D1/30 , B01D3/00 , C02F1/04
CPC分类号： B01D1/007 , B01D1/0047 , B01D1/12 , B01D1/305 , B01D3/007 , C02F1/045 , Y02A20/128
摘要： PCT No. PCT/EP95/03476 Sec. 371 Date Feb. 28, 1997 Sec. 102(e) Date Feb. 28, 1997 PCT Filed Sep. 4, 1995 PCT Pub. No. WO96/07460 PCT Pub. Date Mar. 14, 1996In a method for the desalination of seawater, there is evaporated and condensed the seawater, within a primary system, and a secondary medium, preferentially untreated water, within a compressor-containing, self-contained secondary system spatially separated from the primary system. The seawater is evaporated by heating in the presence of the secondary medium previously heated in the compressor at excess pressure, the latter medium is evaporated in the secondary system through condensation of the seawater vapour and the seawater vapour is led through a cyclone separator. The total seawater flow supplied to the primary system is subdivided into a first component flow and a second component flow of at least approximately equal magnitude, the first component flow, in a first heat transfer unit through which flows the hot water distillate at the output of the primary system, and the second component flow, in a second heat transfer unit through which flows the discharged hot wash-out, being brought to a temperature approaching the boiling temperature in the primary system. A value between greater than 1 and less than 2 is chosen for the ratio of supplied total seawater quantity per unit of time to wash-out quantity per unit of time (concentration factor CF). A method of this kind is suitable for thermal seawater desalination, enabling the production of germ-free water distillate of high quality under simultaneously lesser concentration of the seawater being evaporated and nonetheless saving energy.

5. 发明专利

JPS591376B2 JPS591376B2 - 失效
公开(公告)号：JPS591376B2
公开(公告)日：1984-01-11
申请号：JP14047280
申请日：1980-10-09
申请人： Kogyo Gijutsuin
发明人： YAMAZAKI HARUYUKI , AKATSU YASUAKI , SAKAGUCHI HARUICHIRO
IPC分类号： B01J7/02 , B01D1/12 , B04C7/00 , B04C9/00 , F22B3/02 , F22B37/32
CPC分类号： F22B3/02 , B01D1/12 , B04C7/00 , B04C9/00 , F22B37/322

6. 发明专利

JP2003024701A Circulating evaporator having chamber 审中-公开
标题翻译：具有室的循环蒸发器
公开(公告)号：JP2003024701A
公开(公告)日：2003-01-28
申请号：JP2002146393
申请日：2002-05-21
申请人： Bayer Ag , バイエルアクチェンゲゼルシャフト
发明人： KUPPER KURT-MANFRED , FELLHOELTER ANDRE
IPC分类号： B01D5/00 , B01D1/00 , B01D1/12 , B01D3/00 , B01D3/10 , C08G18/82
CPC分类号： B01D1/12 , B01D1/0094 , B01D3/10 , Y10S159/16 , Y10S159/901
摘要： PROBLEM TO BE SOLVED: To provide a circulating evaporator capable of lowering evaporation temperature and capable of reducing heating quantity to a mixture consisting of a component having higher volatility and a component having lower volatility. SOLUTION: The circulating evaporator has an evaporator, the discharge container connected to the evaporator through a connection piece, a condenser, a vacuum pump, a recirculation line connecting the discharge container to the evaporator and having a pump, a supply line for a raw material mixture and an outflow line for a refined mixture. The discharge container has at least a supply chamber and an outflow chamber, and the outflow chamber to which the outflow line for the refined mixture is connected is directly connected to the connection piece in order to discharge a non-evaporative liquid from the everporator. The supply chamber communicating with the supply line for the raw material mixture is directly connected to the condenser.
摘要翻译：要解决的问题：提供一种能够降低蒸发温度并能够减少由挥发性较高的组分和挥发性低的组分组成的混合物的循环蒸发器。解决方案：循环蒸发器具有蒸发器，排放容器通过连接件，冷凝器，真空泵，连接排放容器到蒸发器的再循环管线连接到蒸发器，并具有泵，用于原料的供应管线混合物和用于精制混合物的流出管线。排出容器至少具有供给室和流出室，并且与精制混合物的流出管连接的流出室直接连接到连接件，以从永久物排放非蒸发性液体。与原料混合物的供给管路连通的供给室与冷凝器直接连接。

7. 发明专利

JPS6115721B2 JPS6115721B2 - 失效
公开(公告)号：JPS6115721B2
公开(公告)日：1986-04-25
申请号：JP7850582
申请日：1982-05-12
申请人： Esmil Bv
发明人： DEITSUKU GERITO KURAREN
IPC分类号： B01D1/06 , B01D1/12 , C02F1/04 , F28D13/00 , F28F13/00 , F28F19/00
CPC分类号： B01D1/065 , B01D1/12 , F28D13/00 , F28F13/00 , F28F19/00 , Y10S159/03

8. 发明专利

JPS59125390A Heat exchanger 失效
标题翻译：热交换器
公开(公告)号：JPS59125390A
公开(公告)日：1984-07-19
申请号：JP23220382
申请日：1982-12-30
申请人： Kuraray Co Ltd
发明人： KOMATSU SHIGERU
IPC分类号： F28F13/00 , B01D1/12 , B01D1/14 , F28D7/16 , F28F13/12
CPC分类号： B01D1/12 , B01D1/14
摘要： PURPOSE:To make use of a calorific value of waste gas of a high temperature for evaporation and heating of raw sewage effectively, by a method wherein gas-liquid direct contact between waste gas of the high temperature and a liquid is made to carry out, and an air lift effect to be generated by blowing gas into a liquid and a circulation flow to be generated resulting from the air lift effect are put to use. CONSTITUTION:When raw sewage is poured into heat exchanger tubes 6, 7 and air is blown into them from an air blow tube 8, gas-liquid direct contact is made between the raw sewage existing within the tubes and the air, which are ascended in an annular part placed between the inside of the large diameter tube 6 and the outside of the blow tube 8 as a mixture flow of the raw sewage and the air by air lift action, heat is given to the mixture flow by the raw sewage, a part of the raw sewage is made to evaporate, the raw sewage is separated from the air in an upper space 9 of an upper tube plate 4, accompanied liquid drops are separated from the air by a collision plate 10, and the air humidified by the raw sewage passed through an air outlet 11 is used as the air for combustion. The raw sewage separated from the air, descended rapidly within the small caliber tube 7 and entered into the large diameter tube 6 is turned into an ascending flow, through which severe circulation flow of the raw sewage is generated, which is cooled through evaporation and heating of the blowing-in air and a cycle of cooling and heating is made on a wall of the tube at the time of descent in the small caliber tube 7 and ascent at the lower part in the large caliber tube 6.
摘要翻译：目的：为了有效地利用高温废气的热值蒸发和加热原污水，通过使高温废气与液体之间的气液直接接触进行的方法，并且使用通过将气体吹入液体而产生的空气提升效果以及由空气提升效果产生的循环流动。构成：当原料污水倒入热交换器管6,7中，空气从吹气管8吹入时，在管内存在的原污水和空气之间进行气液直接接触，作为原料污水和空气通过空气提升作用的混合流动而放置在大直径管6的内部和吹塑管8的外部之间的环形部分，由原料污水向混合物流供给热量原料污水的一部分被蒸发，原料污水在上管板4的上部空间9中与空气分离，伴随着液滴通过碰撞板10与空气分离，并且由作为燃烧用空气，使用通过出气口11的原料污水。与空气分离的原污水在小口径管7内快速下降并进入大直径管6，变成上升流，生成污水的严重循环流动，通过蒸发和加热冷却并且在小口径管7下降时在管的壁上形成冷却和加热循环并在大口径管6的下部上升。

9. 发明专利

JPS5765323A Vapor generator of low boiling point medium 失效
标题翻译：低沸点点蒸汽发生器
公开(公告)号：JPS5765323A
公开(公告)日：1982-04-20
申请号：JP14047280
申请日：1980-10-09
申请人： Agency Of Ind Science & Technol
发明人： YAMAZAKI HARUYUKI , AKATSU YASUAKI , SAKAGUCHI HARUICHIROU
IPC分类号： B01J7/02 , B01D1/12 , B04C7/00 , B04C9/00 , F22B3/02 , F22B37/32
CPC分类号： F22B3/02 , B01D1/12 , B04C7/00 , B04C9/00 , F22B37/322
摘要： PURPOSE: To carry out mixing of a two component mixture and a low b.p. liquid medium well by a method wherein an apparatus used both as a cyclone separator and a heat exchanger is provided and a gas-liquid two phase stream is passed through the low b.p. liquid medium to prevent pyrolysis of vapor of the low b.p. liquid medium.
CONSTITUTION: A two component mixture 101 from a lower header 14 is introduced into a raising pipe 16 and heated by a heating gas 104 to generate vapor 102 of a low b.p. liquid medium. In this condition, a gas-liquid two phase stream 105 of the two component mixture 101 and the vapor 102 of the low b.p. liquid medium is raised through the raising pipe 16 and introduced into a duct 20 of an upper header 12. Said two phase stream is passed through a direct type heat exchanger 28 and contacted with the low b.p. liquid medium 103 from a supply pipe 26 to carry out heat exchanging therebetween and, at the same time, to carry out gas- liquid separation. The separated vapor 102 of the low b.p. liquid medium is discharged from an exhaust pipe 24 and the two component mixture 101 is transferred to the lower header from a descending pipe 18 and recirculated naturally.
COPYRIGHT: (C)1982,JPO&Japio
摘要翻译：目的：进行双组分混合物的混合和低沸点液体介质井，其中提供了用作旋风分离器和热交换器的装置，并且使气液两相流通过低沸点。液体介质，以防止蒸气裂解低沸点。液体介质。构成：来自下集流管14的两组分混合物101被引入升管16中并被加热气体104加热以产生低沸点的蒸汽102。液体介质。在这种情况下，双组分混合物101的气液两相流105和低沸点的蒸气102。液体介质通过提升管16升高并被引入上集流管12的管道20中。所述两相流通过直接型热交换器28并与低沸点温度接触。液体介质103从供给管26进行热交换，同时进行气液分离。分离的蒸气102低沸点液体介质从排气管24排出，并且两个组分混合物101从下降管18转移到下部集管并自然地再循环。

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