JP3611514B2 - Salt making apparatus and seawater concentration apparatus - Google Patents

Salt making apparatus and seawater concentration apparatus Download PDF

Info

Publication number
JP3611514B2
JP3611514B2 JP2000317560A JP2000317560A JP3611514B2 JP 3611514 B2 JP3611514 B2 JP 3611514B2 JP 2000317560 A JP2000317560 A JP 2000317560A JP 2000317560 A JP2000317560 A JP 2000317560A JP 3611514 B2 JP3611514 B2 JP 3611514B2
Authority
JP
Japan
Prior art keywords
salt
seawater
heating device
making chamber
salt making
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.)
Expired - Lifetime
Application number
JP2000317560A
Other languages
Japanese (ja)
Other versions
JP2002128519A (en
Inventor
英雄 平良
Original Assignee
英雄 平良
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 英雄 平良 filed Critical 英雄 平良
Priority to JP2000317560A priority Critical patent/JP3611514B2/en
Publication of JP2002128519A publication Critical patent/JP2002128519A/en
Application granted granted Critical
Publication of JP3611514B2 publication Critical patent/JP3611514B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Seasonings (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、製塩装置及び海水濃縮装置に関する。
【0002】
【従来の技術】
従来、わが国の食用塩としては、イオン交換樹脂膜法により製造される精製塩や、塩田等を用いて海水を自然に濃縮・蒸発させて結晶化して製造する自然塩等が知られている。精製塩は、塩化ナトリウムの純度が99%以上の精白塩であり、海水中に含まれる多くのミネラル成分(カルシウムイオン、カリウムイオン、硫酸イオン、マグネシウムイオン等)は製造過程において除去されるので、ほとんど含まれていない。
【0003】
これに対して、自然塩はミネラル含有率が高く、銘柄によっては塩化ナトリウムの純度が92%以下でミネラル成分が8%以上のものもある。このミネラル成分は人体に必須の微量元素であるばかりでなく、塩に苦みと甘味を与え、料理に旨味を加えるとされ、プロの料理人に使用されることが多い。また、自然塩が含むミネラル成分は、他の食物から摂取されるミネラル成分とは異なり、人体への吸収が非常に良好で健康に良いとされている。
【0004】
【発明が解決しようとする課題】
自然塩の製造方法としては、例えば、自然の力(太陽光、風力等)を利用して海水中の水分をとばして濃縮させ、その後加熱して水分を蒸発させるという方法が知られているが、こうした方法は効率が悪く、したがってコストのかかるものであった。
【0005】
本願発明は上記の点にがんみてなされたもので、海水から自然塩を効率良く製塩したり、また海水を効率良く濃縮したりする装置を提供することを課題とする。
【0006】
【課題を解決するための手段】
上記課題を解決するため、本発明においては、加熱装置を配置した製塩室と、製塩室内に海水を噴霧する手段とによって製塩装置を構成し、加熱装置に放熱板を設けるようにした。
【0007】
また、上記原理は海水濃縮装置にも適用できる。すなわち、本発明の海水濃縮装置は、加熱装置を配置した製塩室と、製塩室内に海水を噴霧する手段と、噴霧後の海水を循環させる手段とによって構成され、加熱装置に放熱板を設けるようにした。
【0008】
【発明の実施の形態】
図1は本発明の第1の実施形態を示す平面図、図2は図1のA−A線に沿った断面図、図3は図1のB−B線に沿った断面図である。製塩装置1は、製塩室3と、製塩室3内に配置した加熱装置5と、製塩室3内に海水を噴霧する噴霧ノズル7とを備えている。製塩室3は家屋9内に構成され、家屋9の底面には車輪13が取り付けられ、移動式家屋となっている。もちろん、車輪13を外して固定式にしてもよい。移動式にすれば、場所を選ばず、どのような地域や土地にも設置することができるので利便性が向上する。
【0009】
家屋9の床15には加熱装置5が設置されている。加熱装置5は、金属製(例えばステンレス製)で切妻屋根をもった家屋形状をしており、その内部は中空となっていて、木炭、木材、その他の可燃物を収容して燃焼させ、その熱を製塩室3内へ放出する。燃料は投入口17から投入され、燃焼ガスは煙突18(図2)から排出される。加熱装置5の側面には、空気取入口20(図4)が形成され、この空気取入口20へダクト22(図1〜3)を介して室外から空気が導入される(ただし図5ではダクトを省略)。加熱装置5の切妻屋根19(図4)には、金属製の放熱板21が複数枚取り付けられ、放熱効果を向上させている。
【0010】
上記のような加熱装置5を使用すれば、室内3を例えば120゜C以上の高温にすることが可能であり、その中に噴霧ノズル7から海水を噴霧すると海水中の水分は瞬時に蒸発して、海水成分は塩として結晶化され落下する。なお、加熱装置5の形状は図4に記載されたもの(家屋形式)に限定されない。加熱装置5の形状は、燃料によっても異なり、例えば、ガス、石油、電気等の燃料を使用する場合は、それに応じた形状にすればよい。また、放熱板の形状は、加熱装置5の形状に応じて決めればよく、要するに加熱装置5の熱が製塩室3内に効率良く放出されるものであれば、どのような形状であってもよい。
【0011】
噴霧ノズル7は、市販の噴霧ノズルを使用することができ、家屋9の両側の側壁9aに配管されたパイプ23に、製塩室3内側へ向けて複数個取り付けられている。パイプ23は、海水パイプ25に連結され、海水パイプ25は海水タンク(図示せず)と連絡され、貯蔵した海水が供給される。噴霧ノズル7としてはどのようなタイプのものを使用してもよい。例えば、ノズル7の内部に防錆性のステンレス網からなるフィルタが収納され、このフィルタによって海水中のゴミ等の不純物を除去できるようにし、フィルタが目詰りを起こしたときには簡単に取替えられるタイプのものを使用してもよい。
【0012】
加熱装置5の両側には、結晶化した塩を搬送するベルトコンベア27が配置され、各ベルトコンベア27,27の両サイドには、落下した塩をベルトコンベア27へ回収するための傾斜板29が配置されている。ベルトコンベア27の終端には塩受け31が配置されている。ベルトコンベア27の両サイドの傾斜板29,29のうち、内側(加熱装置5寄り)の傾斜板29は、加熱装置5の屋根19の直下からベルトコンベア27にかけて配置され、外側(側壁9a寄り)の傾斜板29は側壁9aからベルトコンベア27にかけて配置されている。しかし、傾斜板29を設けずに屋根19の直下にベルトコンベア27を配置してもよい。側壁9aの下部には、外気取入口33が設けられ、家屋9の屋根部には換気口35が設けられ、外気取入口33,換気口35はそれぞれ虫避けのための防虫網で覆われている。
【0013】
次に、上記製塩装置1の動作について説明する。
まず、あらかじめ加熱装置5に燃料を投入して燃焼させ、室内3の温度を例えば120゜C 程度に上昇させる。加熱装置5は複数の放熱板21を有しているので熱は効率良く製塩室3内へ放出され、室内は短時間で高温に達する。次いで、海水パイプ25へ海水を導入し噴射ノズル7を介して海水を製塩室3内へ噴霧する。製塩室3内に噴霧された海水は、高温のため水分が蒸発し、結晶化して塩となって落下する。加熱装置5の屋根19上に落下した塩は屋根19、傾斜板29を介してベルトコンベア27まで滑り落ち、その後ベルトコンベア27によって搬送され、塩受け31に回収される。なお、製塩室3内へは外気取入口33から空気が取り入れられ、換気口35から出ていくという空気の流れが形成されており、それにより蒸発した水分は換気口35から室外へ放出される。なお、換気口35には、排気用の換気扇を取り付けるようにしてもよい。
【0014】
上述したように、加熱装置5の屋根19は勾配をもった形状になっているので、加熱装置5上に落下した塩は屋根に付着することなくベルトコンベア27上へ更に落下され、効率良く収集される。屋根の勾配θは、特に限定されないが、勾配θを小さくするほど塩が屋根19につもりにくくなる。一例としては、θ=45゜以下にすると塩が屋根19につもりにくい。また、ベルトコンベア27を利用しているので、作業員が製塩室3内に入ることなく塩を回収でき、極めて衛生的である。なお、ベルトコンベア27を使用せずに、人力で塩を回収してもよく、その場合は、例えば熊手状(T字型)の器具を使用して塩を室外へかき出すようにしてもよい。このとき、器具は製塩室内に置いて作業員は室内に入らずに製塩室の出入口側から器具を操作して塩をかき出すようにするとよい。
【0015】
図5は、本発明の第2の実施形態を示し、ここでは、上記製塩装置1と同じ原理を用いて、海水濃縮装置37を構成した。すなわち、海水濃縮装置37は、製塩装置1の製塩室3内の温度を低めに設定して(例えば50゜C程度)、海水を結晶化させず、噴霧した海水を回収して循環させて海水の塩分濃度を高める。上記製塩装置1と異なる点は、ベルトコンベア27に代えて、海水の循環路を設けたことである。海水の循環路は、家屋9の床部分に設けた勾配をつけた床39、床39を伝わって流下する海水を受ける受溝41、受溝41と連結された送水管43、送水管43からの濃縮海水を貯蔵する貯蔵タンク45、貯蔵タンク45の濃縮海水を還流させる揚水ポンプ47、揚水ポンプ47と海水パイプ25と連絡する送水管49とから構成される。その他の構成は、上記製塩装置1と同様である。
【0016】
上記のような海水濃縮装置37を用いれば、海水の噴霧、循環、再噴霧を繰り返すことにより、効率良く海水を濃縮することができる。この濃縮装置装置37は、深層水等の商品価値のある海水を輸送する際、海水を濃縮するときに使用することができる。濃縮した海水は体積、重量ともに小さくなるので、輸送コストを低減させることができ、それにより、深層水を用いた製品のコストを大幅に低減させることが可能となる。
【0017】
【発明の効果】
以上説明したように、本発明によれば、海水から自然塩を効率良く製塩したり、海水を効率良く濃縮したりすることができる。
【図面の簡単な説明】
【図1】製塩装置の平面図。
【図2】図1のA−A線に沿った断面図。
【図3】図1のB−B線に沿った断面図。
【図4】加熱装置の斜視図。
【図5】海水濃縮装置の概略図。
【符号の説明】
1 製塩装置
3 製塩室
5 加熱装置
7 噴霧ノズル
21 放熱板
37 海水濃縮装置
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a salt making apparatus and a seawater concentration apparatus.
[0002]
[Prior art]
Conventionally, as edible salt in Japan, a purified salt produced by an ion exchange resin membrane method, a natural salt produced by crystallization by naturally concentrating and evaporating seawater using a salt pad etc. are known. The refined salt is a refined salt with a purity of 99% or more of sodium chloride, and many mineral components (calcium ions, potassium ions, sulfate ions, magnesium ions, etc.) contained in seawater are removed during the production process. It is hardly included.
[0003]
On the other hand, natural salt has a high mineral content, and some brands have a sodium chloride purity of 92% or less and a mineral component of 8% or more. This mineral component is not only an essential trace element for the human body, but also gives bitterness and sweetness to salt and adds umami to cooking, and is often used by professional cooks. Moreover, the mineral component which natural salt contains is considered to be very good for health and absorption to a human body unlike the mineral component ingested from other foods.
[0004]
[Problems to be solved by the invention]
As a method for producing natural salt, for example, a method is known in which natural power (sunlight, wind power, etc.) is used to condense and condense water in seawater, and then heat to evaporate the water. These methods were inefficient and therefore costly.
[0005]
The present invention has been made with the above points in mind, and it is an object of the present invention to provide an apparatus for efficiently producing natural salt from seawater or efficiently concentrating seawater.
[0006]
[Means for Solving the Problems]
In order to solve the above problems, in the present invention, a salt making apparatus is constituted by a salt making chamber in which a heating device is disposed and means for spraying seawater into the salt making chamber, and a heat radiating plate is provided in the heating device.
[0007]
The above principle can also be applied to seawater concentrators. That is, the seawater concentrating device of the present invention is constituted by a salt making chamber in which a heating device is arranged, means for spraying seawater into the salt making chamber, and means for circulating the seawater after spraying, and the heating device is provided with a heat sink. I made it.
[0008]
DETAILED DESCRIPTION OF THE INVENTION
FIG. 1 is a plan view showing a first embodiment of the present invention, FIG. 2 is a cross-sectional view taken along line AA in FIG. 1, and FIG. 3 is a cross-sectional view taken along line BB in FIG. The salt making apparatus 1 includes a salt making chamber 3, a heating device 5 disposed in the salt making chamber 3, and a spray nozzle 7 that sprays seawater into the salt making chamber 3. The salt making room 3 is configured in a house 9, and wheels 13 are attached to the bottom surface of the house 9 to form a mobile house. Of course, the wheel 13 may be removed and fixed. If it is mobile, it can be installed in any area or land regardless of location, so convenience is improved.
[0009]
The heating device 5 is installed on the floor 15 of the house 9. The heating device 5 has a house shape made of metal (for example, made of stainless steel) and has a gable roof. The inside of the heating device 5 is hollow, and contains charcoal, wood, and other combustible materials for combustion. Heat is released into the salt making chamber 3. The fuel is input from the input port 17, and the combustion gas is discharged from the chimney 18 (FIG. 2). An air intake 20 (FIG. 4) is formed on the side surface of the heating device 5, and air is introduced into the air intake 20 from the outside through a duct 22 (FIGS. 1 to 3) (however, in FIG. Omitted). A plurality of metal heat sinks 21 are attached to the gable roof 19 (FIG. 4) of the heating device 5 to improve the heat dissipation effect.
[0010]
If the heating device 5 as described above is used, the room 3 can be heated to a high temperature of, for example, 120 ° C. or more, and when seawater is sprayed from the spray nozzle 7, the water in the seawater is instantly evaporated. The seawater component is crystallized and dropped as salt. In addition, the shape of the heating apparatus 5 is not limited to what was described in FIG. 4 (house form). The shape of the heating device 5 varies depending on the fuel. For example, when a fuel such as gas, petroleum, electricity, or the like is used, the shape may be set accordingly. The shape of the heat sink may be determined according to the shape of the heating device 5. In short, any shape can be used as long as the heat of the heating device 5 is efficiently released into the salt making chamber 3. Good.
[0011]
A commercially available spray nozzle can be used as the spray nozzle 7, and a plurality of spray nozzles 7 are attached to the inside of the salt making chamber 3 on the pipes 23 piped on the side walls 9 a on both sides of the house 9. The pipe 23 is connected to a seawater pipe 25. The seawater pipe 25 is connected to a seawater tank (not shown), and stored seawater is supplied. Any type of spray nozzle 7 may be used. For example, a filter made of a rust-proof stainless steel net is housed in the nozzle 7 so that impurities such as dust in seawater can be removed by this filter, and can be easily replaced when the filter is clogged. Things may be used.
[0012]
Belt conveyors 27 for conveying crystallized salt are disposed on both sides of the heating device 5, and inclined plates 29 for collecting the dropped salt to the belt conveyor 27 are disposed on both sides of each belt conveyor 27, 27. Has been placed. A salt receiver 31 is disposed at the end of the belt conveyor 27. Of the inclined plates 29 and 29 on both sides of the belt conveyor 27, the inclined plate 29 on the inner side (closer to the heating device 5) is disposed from directly below the roof 19 of the heating device 5 to the belt conveyor 27, and is outer (closer to the side wall 9a). The inclined plate 29 is arranged from the side wall 9 a to the belt conveyor 27. However, the belt conveyor 27 may be disposed directly below the roof 19 without providing the inclined plate 29. An outside air inlet 33 is provided at the lower portion of the side wall 9a, and a ventilation opening 35 is provided at the roof portion of the house 9. The outside air inlet 33 and the ventilation opening 35 are each covered with an insect net for preventing insects. Yes.
[0013]
Next, the operation of the salt making apparatus 1 will be described.
First, the fuel is introduced into the heating device 5 and burned in advance, and the temperature of the room 3 is raised to, for example, about 120 ° C. Since the heating device 5 has a plurality of heat radiation plates 21, heat is efficiently released into the salt making chamber 3, and the room reaches a high temperature in a short time. Next, seawater is introduced into the seawater pipe 25, and the seawater is sprayed into the salt making chamber 3 through the injection nozzle 7. The seawater sprayed in the salt making chamber 3 evaporates due to the high temperature, crystallizes and falls as salt. The salt dropped on the roof 19 of the heating device 5 slides down to the belt conveyor 27 through the roof 19 and the inclined plate 29, and is then conveyed by the belt conveyor 27 and collected in the salt receiver 31. In addition, air is introduced into the salt making chamber 3 from the outside air inlet 33 and exits from the ventilation port 35, whereby the evaporated water is discharged from the ventilation port 35 to the outside of the room. . A ventilation fan for exhaust may be attached to the ventilation port 35.
[0014]
As described above, since the roof 19 of the heating device 5 has a gradient shape, the salt dropped on the heating device 5 is further dropped onto the belt conveyor 27 without adhering to the roof, and is efficiently collected. Is done. The slope θ of the roof is not particularly limited, but the salt becomes less likely to be on the roof 19 as the slope θ is decreased. As an example, when θ = 45 ° or less, salt is unlikely to be on the roof 19. Further, since the belt conveyor 27 is used, the worker can collect the salt without entering the salt making chamber 3 and is extremely hygienic. In addition, you may collect | recover salt manually without using the belt conveyor 27, and in that case, you may make it skim out of salt using a rake-like (T-shaped) instrument, for example. At this time, it is preferable that the instrument is placed in the salt making room and the operator operates the instrument from the entrance / exit side of the salt making room to scoop out the salt without entering the room.
[0015]
FIG. 5 shows a second embodiment of the present invention, in which a seawater concentrating device 37 is configured using the same principle as the salt making device 1 described above. That is, the seawater concentrating device 37 sets the temperature in the salt making chamber 3 of the salt making device 1 to be low (for example, about 50 ° C.), collects and circulates the sprayed seawater without crystallizing the seawater, Increase the salinity of. The difference from the salt making apparatus 1 is that a seawater circulation path is provided in place of the belt conveyor 27. The seawater circulation path includes a sloped floor 39 provided on the floor portion of the house 9, a receiving groove 41 for receiving seawater flowing down the floor 39, a water supply pipe 43 connected to the receiving groove 41, and a water supply pipe 43. A storage tank 45 for storing the concentrated seawater, a pumping pump 47 for refluxing the concentrated seawater in the storage tank 45, a pumping pump 47, and a water supply pipe 49 communicating with the seawater pipe 25. Other configurations are the same as those of the salt making apparatus 1 described above.
[0016]
By using the seawater concentrator 37 as described above, seawater can be efficiently concentrated by repeating spraying, circulation, and respraying of seawater. This concentrating device 37 can be used when concentrating seawater when transporting seawater having commercial value such as deep water. Since the concentrated seawater is small in both volume and weight, the transportation cost can be reduced, and thereby the cost of the product using the deep water can be greatly reduced.
[0017]
【The invention's effect】
As described above, according to the present invention, natural salt can be efficiently produced from seawater or seawater can be efficiently concentrated.
[Brief description of the drawings]
FIG. 1 is a plan view of a salt making apparatus.
2 is a cross-sectional view taken along line AA in FIG.
3 is a cross-sectional view taken along line BB in FIG.
FIG. 4 is a perspective view of a heating device.
FIG. 5 is a schematic view of a seawater concentration apparatus.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Salt making apparatus 3 Salt making chamber 5 Heating apparatus 7 Spray nozzle 21 Heat sink 37 Seawater concentration apparatus

Claims (4)

加熱装置を配置した製塩室と、前記製塩室内に海水を噴霧する手段とを備え、前記加熱装置は、前記製塩室内への放熱効果を向上させるための放熱板を備えたことを特徴とする製塩装置。A salt making chamber provided with a heating device; and means for spraying seawater into the salt making chamber, wherein the heating device includes a heat radiating plate for improving a heat radiation effect into the salt making chamber. apparatus. 前記加熱装置に傾斜屋根を設けた請求項1に記載の製塩装置。The salt making apparatus of Claim 1 which provided the inclined roof in the said heating apparatus. 前記傾斜屋根の下方に結晶化した塩を搬送する搬送手段を設けた請求項2に記載の製塩装置。The salt making apparatus of Claim 2 which provided the conveyance means to convey the crystallized salt under the said inclined roof. 加熱装置を配置した製塩室と、前記製塩室内に海水を噴霧する手段と、噴霧後の海水を循環させる手段とを備え、前記加熱装置は、前記製塩室内への放熱効果を向上させるための放熱板を備えたことを特徴とする海水濃縮装置。A salt-making chamber in which a heating device is arranged; means for spraying seawater into the salt-making chamber; and means for circulating seawater after spraying; and the heating device dissipates heat to improve the heat dissipation effect into the salt-making chamber. A seawater concentration apparatus comprising a plate.
JP2000317560A 2000-10-18 2000-10-18 Salt making apparatus and seawater concentration apparatus Expired - Lifetime JP3611514B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000317560A JP3611514B2 (en) 2000-10-18 2000-10-18 Salt making apparatus and seawater concentration apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000317560A JP3611514B2 (en) 2000-10-18 2000-10-18 Salt making apparatus and seawater concentration apparatus

Publications (2)

Publication Number Publication Date
JP2002128519A JP2002128519A (en) 2002-05-09
JP3611514B2 true JP3611514B2 (en) 2005-01-19

Family

ID=18796326

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000317560A Expired - Lifetime JP3611514B2 (en) 2000-10-18 2000-10-18 Salt making apparatus and seawater concentration apparatus

Country Status (1)

Country Link
JP (1) JP3611514B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101886682B1 (en) * 2018-02-13 2018-09-10 이양우 A manufacturing device of high salinity seawater

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101420566B1 (en) * 2013-03-20 2014-08-13 김진호 Manufacturing apparatus of salt using micro mist spray

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101886682B1 (en) * 2018-02-13 2018-09-10 이양우 A manufacturing device of high salinity seawater
KR20190098015A (en) * 2018-02-13 2019-08-21 이양우 A manufacturing device of high salinity seawater
KR102071276B1 (en) * 2018-02-13 2020-01-30 이양우 A manufacturing device of high salinity seawater

Also Published As

Publication number Publication date
JP2002128519A (en) 2002-05-09

Similar Documents

Publication Publication Date Title
US11623177B2 (en) Atmospheric water generation systems and methods
US6165326A (en) Facility for desalinating of purifying sea water or brackish water by means of solar energy
JP3250738B2 (en) Seawater treatment method and treatment equipment, natural salt and freshwater
US6868690B2 (en) Production of potable water and freshwater needs for human, animal and plants from hot and humid air
RU2465220C2 (en) Device and method of drying water-bearing material
TWI227163B (en) Method and apparatus for simultaneous heat and mass transfer utilizing a carrier-gas
US20220195706A1 (en) Atmospheric water generation systems and methods
KR20160060283A (en) Photovoltaics system to able seawater desalination
Thanaiah et al. Experimental analysis on humidification-dehumidification desalination system using different packing materials with baffle plates
JP3611514B2 (en) Salt making apparatus and seawater concentration apparatus
CN108476987A (en) A kind of environment-friendly temperature-reducing pig house
CN102381735A (en) Semi-dry process air humidifying and dehumidifying type seawater desalinating system and method
CN206858200U (en) A kind of new evaporation concentration system that hc effluent is handled using fume afterheat
US9227853B2 (en) Desalination unit for the production of potable water from sub-soil brine
JP3030693B2 (en) Sea salt production apparatus and method
CN109704504A (en) A kind of comprehensive deliverance apparatus of Oversea wind power generation
CN103241786A (en) Evaporation system
CN110316779B (en) High-efficiency energy-saving brackish water/seawater desalination device
KR20100075803A (en) Fresh water making device
CN209835928U (en) Intelligent drying system for sludge after sewage treatment
CN106922813A (en) A kind of thawing apparatus of frozen squid
CN203269605U (en) Evaporation system
CN210057409U (en) Enrichment facility is used in water-soluble fertile production
CN212132489U (en) Flue gas waste heat recovery system
JPS6193885A (en) Seawater desalting apparatus

Legal Events

Date Code Title Description
TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20040929

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20041019

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

Ref document number: 3611514

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20071029

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101029

Year of fee payment: 6

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101029

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111029

Year of fee payment: 7

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111029

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121029

Year of fee payment: 8

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121029

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20131029

Year of fee payment: 9

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250