JPH087031B2 - Cooling method for high viscosity liquid - Google Patents

Cooling method for high viscosity liquid

Info

Publication number
JPH087031B2
JPH087031B2 JP1936387A JP1936387A JPH087031B2 JP H087031 B2 JPH087031 B2 JP H087031B2 JP 1936387 A JP1936387 A JP 1936387A JP 1936387 A JP1936387 A JP 1936387A JP H087031 B2 JPH087031 B2 JP H087031B2
Authority
JP
Japan
Prior art keywords
cooling water
temperature
passage
cooling
heat transfer
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 - Fee Related
Application number
JP1936387A
Other languages
Japanese (ja)
Other versions
JPS63279099A (en
Inventor
洋一 加藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hisaka Works Ltd
Original Assignee
Hisaka Works Ltd
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 Hisaka Works Ltd filed Critical Hisaka Works Ltd
Priority to JP1936387A priority Critical patent/JPH087031B2/en
Publication of JPS63279099A publication Critical patent/JPS63279099A/en
Publication of JPH087031B2 publication Critical patent/JPH087031B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 産業上の利用分野 この発明はプレート式熱交換器に関し、より具体的に
は粘度の高い液体の冷却を扱うプレート式冷却装置に関
するもので、各種の樹脂、油脂、ワニス・ビスコース等
の紡糸液、糖液、食品用流体、乳製品等々、従来プレー
ト式ではかなり困難とされていた超高粘度の液体の冷却
に応用しうるものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a plate heat exchanger, and more particularly to a plate cooling device that handles cooling of a highly viscous liquid, including various resins, oils and fats, and varnishes. It can be applied to the cooling of ultra-high viscosity liquid, which has been considered to be quite difficult with the conventional plate type, such as spinning solutions such as viscose, sugar solutions, food fluids and dairy products.

従来の技術および発明が解決しようとする問題点 プレート式熱交換器は、周知の通り、伝熱板を介して
隣り合った通路にそれぞれ流体を供給してこれらの流体
相互間で間接的に熱交換を行わせるようにしたものであ
る。
2. Description of the Related Art As is well known, plate type heat exchangers supply fluids to adjacent passages via heat transfer plates to indirectly generate heat between these fluids. It is designed to be exchanged.

しかして一般に伝熱性能とりわけ冷却能力についてみ
ると、冷却水温度が低いほど、また冷却水量が多いほ
ど、冷却効果が高いというのが技術常識である。ところ
が、粘度の高い液体の冷却に関する限り、これは必ずし
も当てはまらないことが判明した。すなわち、冷却水と
して通常の工業用水(水温25℃〜30℃程度)を用いて実
験をしたところによると、処理液側の伝熱および流動性
能が冷却水側の温度に大きく支配され、特に流動性が極
端に悪くなって圧力損失が大幅に増加し、殆ど流れなく
なってしまうという事態が確認された。
However, generally, regarding the heat transfer performance, especially the cooling capacity, it is common general knowledge that the cooling effect is higher as the cooling water temperature is lower and the cooling water amount is higher. However, it has been found that this is not always the case, as far as cooling viscous liquids is concerned. That is, according to an experiment using normal industrial water (water temperature of about 25 ° C to 30 ° C) as cooling water, heat transfer and flow performance on the treatment liquid side are largely controlled by the temperature on the cooling water side, and It was confirmed that the property became extremely poor and the pressure loss increased significantly, causing almost no flow.

伝熱板を隔てて隣接する各通路での冷却水温度と伝熱
および流動性の関係についてみるならば、第2図に示す
ように、冷却水温度をt→t′→t″と下げると、これ
に近似して高粘度液と接する壁面温度もTw→Tw′→Tw″
と下がる。この結果、伝熱板の壁面に近い部分では高粘
度液の粘度が急激に増大し、通路内の速度分布は図に示
す温度分布と概ね同様に変化し、流動性能及び伝熱性能
が著しく損なわれることが看て取れる。
To examine the relationship between the cooling water temperature and the heat transfer and fluidity in each of the passages that are adjacent to each other across the heat transfer plate, lower the cooling water temperature as t → t ′ → t ″ as shown in FIG. , And the temperature of the wall surface in contact with the high-viscosity liquid is also Tw → Tw ′ → Tw ″
And goes down. As a result, the viscosity of the high-viscosity liquid rapidly increases near the wall surface of the heat transfer plate, the velocity distribution in the passage changes almost in the same way as the temperature distribution shown in the figure, and the flow performance and heat transfer performance are significantly impaired. You can see what is going on.

問題点を解決するための手段 この発明は上述の問題点に鑑み、粘度の高い液体の効
果的な冷却方法およびそれに適する実用的なプレート式
冷却装置を提供せんとするもので、処理液と冷却水との
熱交換に際し、冷却水温度を処理液の粘度に見合った適
当な値に調整することによって、処理液の粘度が過度に
高くならないようにして伝熱性能および流動性の向上を
図ることを基本的構想とし、そのために、熱交換により
昇温した冷却水の少なくとも一部を再循環させる。すな
わち、冷却水を冷却水通路の出口側から入口側へ導く循
環通路を設けるとともに、循環量を制御する装置を設け
たものである。
Means for Solving the Problems In view of the above-mentioned problems, the present invention aims to provide an effective cooling method for a highly viscous liquid and a practical plate-type cooling device suitable for the method. When exchanging heat with water, the cooling water temperature is adjusted to an appropriate value corresponding to the viscosity of the treatment liquid so that the viscosity of the treatment liquid does not become excessively high and heat transfer performance and fluidity are improved. The basic idea is to recirculate at least a part of the cooling water heated by heat exchange. That is, a circulation passage for guiding the cooling water from the outlet side to the inlet side of the cooling water passage is provided, and a device for controlling the circulation amount is provided.

作用 処理液と冷却水との間で、伝熱板を介して熱交換が行
われる結果、冷却水は処理液から熱を奪って昇温し、逆
に処理液は熱を奪われて冷却される。斯くして昇温した
冷却水は、新たに補給される冷却水と合流して系内を再
循環する。冷却水は全部再循環させることもできるし所
望の一部だけ再循環させてもよい。いずれにせよ循環量
は、扱う処理液の物性如何に応じて、その粘度を系内流
通および伝熱に支障を来すに至る程増大せしめない程度
で、かつ、所期の冷却性能を確保するに足る適当な冷却
水温度を維持するようにコントロールする。
Action As a result of heat exchange between the treatment liquid and the cooling water via the heat transfer plate, the cooling water takes heat from the treatment liquid and rises in temperature, and conversely the treatment liquid is deprived of heat and cooled. It The cooling water whose temperature has risen in this way merges with the newly supplied cooling water and recirculates in the system. The cooling water may be entirely recirculated or only a desired part thereof may be recirculated. In any case, depending on the physical properties of the treatment liquid to be handled, the circulation amount is such that the viscosity does not increase to the extent that it interferes with internal system flow and heat transfer, and also secures the desired cooling performance. Control to maintain the proper cooling water temperature.

実施例 第1図に示すこの発明の実施例について説明すると、
この実施例の冷却装置は、伝熱板(2)を介して隣り合
う処理液通路(4)と冷却水通路(6)を備えたプレー
ト式熱交換器(8)を含んでいる。伝熱板(2)は、当
該熱交換器に要求される能力に応じて複数枚成層して交
互の通路(4)(6)を形成するなお、図中熱交換器
(8)を構成するプレート群のうち、左半分は冷却水通
路(6)を相互に連絡せしめる通孔(6a)(6a)に沿っ
た断面を示し、右半分は処理液通路(4)を相互に連絡
せしめる通孔(4a)(4a)に沿った断面を示している。
冷却水は一旦補給タンク(10)に貯溜され、そこから入
口配管(12)を通じてポンプ(14)で冷却水通路(6)
へ供給される。冷却水は冷却水通路(6)内を流過する
際、伝熱板(2)を介して、隣位の処理液通路(4)内
の処理液すなわち高粘度液から熱を奪って昇温し、出口
配管(16)へ向かう。出口配管(16)は冷却水を系外へ
導くようになっているが、その途中から循環通路(18)
が分岐してタンク(10)へ通じている。換言すれば、循
環通路(18)は冷却水通路(6)の出口側と入口側とを
連絡している。循環通路(18)には流量制御弁(20)を
取り付け、その開度を冷却水通路(6)に供給すべき冷
却水、つまり図示例の場合タンク(10)内の冷却水の温
度に応じてコントロールするためのサーモコントローラ
(22)を設けてある。
EXAMPLE An example of the present invention shown in FIG. 1 will be described.
The cooling device of this embodiment includes a plate heat exchanger (8) having a treatment liquid passage (4) and a cooling water passage (6) which are adjacent to each other via a heat transfer plate (2). The heat transfer plate (2) is laminated to form a plurality of alternating passages (4) and (6) according to the capacity required for the heat exchanger. The heat exchanger (8) in the figure is formed. Of the plate group, the left half shows a cross section along the through holes (6a) (6a) that connect the cooling water passages (6) to each other, and the right half shows the through holes that connect the processing liquid passages (4) to each other. (4a) shows a cross section along (4a).
The cooling water is once stored in the replenishment tank (10), and then the cooling water passage (6) is pumped through the inlet pipe (12) by the pump (14).
Supplied to When the cooling water flows through the cooling water passage (6), the cooling water draws heat from the processing liquid in the adjacent processing liquid passage (4), that is, the high-viscosity liquid, through the heat transfer plate (2) to raise the temperature. And head for the outlet pipe (16). The outlet pipe (16) guides the cooling water to the outside of the system, and the circulation passage (18)
Branch into the tank (10). In other words, the circulation passage (18) connects the outlet side and the inlet side of the cooling water passage (6). A flow rate control valve (20) is attached to the circulation passage (18), and the opening degree of the flow control valve (20) depends on the temperature of the cooling water to be supplied to the cooling water passage (6), that is, the temperature of the cooling water in the tank (10) in the illustrated example. A thermo controller (22) is provided for controlling the temperature.

しかして、プレート式熱交換器(8)において処理液
から熱を奪って昇温した冷却水を循環通路(18)を通し
てタンク(10)に導き新たな冷却水と合流させることに
より、冷却水通路(6)へ供給される冷却水の温度が高
まる。さらに、当該温度上昇の程度は、流量制御弁(2
0)で冷却水の循環量を制御することによって適宜調整
する。例えば、処理液をその粘度が伝熱および流動に支
障を来すに至らない範囲の温度まで冷却しうる適当な温
度に維持する。斯かる温度コントロールを担う手段とし
ては、自動制御の分野において知られているものの中か
ら随意に選択することができるので、ここではサーモコ
ントローラ(22)からの信号に応答して流量制御弁(2
0)が開閉するようにした例を示すに止める。
Then, in the plate heat exchanger (8), the cooling water, which has taken up heat from the treatment liquid to rise in temperature, is introduced into the tank (10) through the circulation passage (18) and merged with the new cooling water, whereby the cooling water passage is formed. The temperature of the cooling water supplied to (6) increases. Further, the degree of the temperature rise is determined by the flow control valve (2
It is appropriately adjusted by controlling the circulation amount of cooling water in 0). For example, the treatment liquid is maintained at a suitable temperature at which the viscosity can be cooled to a temperature at which the viscosity does not interfere with heat transfer and flow. The means for performing such temperature control can be arbitrarily selected from those known in the field of automatic control, so here, in response to the signal from the thermo controller (22), the flow control valve (2
(0) is shown below as an example of opening and closing.

次表は従来の冷却装置による場合と本発明による場合
とにおける性能比較を具体的数値をもって示したもので
ある。なお、ここに処理液の粘度は100℃で90cp、30℃
で65000cpというものである。
The following table shows the performance comparison between the case of the conventional cooling device and the case of the present invention with specific numerical values. The viscosity of the processing liquid is 90 cp at 100 ° C and 30 ° C.
That's 65,000 cp.

従来はこの工業用水、上水等をそのまま冷却水(27
℃)とに使用している。この結果、従来装置においては
処理液の出口温度が29℃まで過度に冷却されてしまい粘
度が急激に高くなって圧力損失の増大を招き、結果的に
処理流量を流すことが不可能であった。しかるに本発明
では熱交換により昇温(50℃)した冷却水を再循環させ
ることにより48℃まで「加熱」して供給している。この
結果、流動性が良好となり、圧力損失も小さくなり、所
定流量が安定に流れ、供給伝熱係数も略倍増した。
Conventionally, this industrial water, tap water, etc. are used as they are as cooling water (27
(° C) and used. As a result, in the conventional apparatus, the outlet temperature of the processing liquid was excessively cooled to 29 ° C., the viscosity suddenly increased and the pressure loss increased, resulting in the inability to flow the processing flow rate. . In the present invention, however, the cooling water that has been heated (50 ° C.) by heat exchange is recirculated and “heated” to 48 ° C. before being supplied. As a result, the fluidity was improved, the pressure loss was reduced, a predetermined flow rate was stably flowed, and the heat transfer coefficient for supply was also approximately doubled.

発明の効果 この発明によれば粘度の高い液体に対しても流動性を
損なうことなく、優れた伝熱性能を発揮するプレート式
冷却装置が得られ、高粘度もしくは超高粘度の液体の冷
却用途に供しうるプレート式熱交換器の実用化に向けて
寄与することろ大である。しかも別途の熱源に頼ること
なく冷却水の昇温を行うものであるからコスト及び省エ
ネルギーの見地からも極めて有利である。
EFFECTS OF THE INVENTION According to the present invention, it is possible to obtain a plate-type cooling device that exhibits excellent heat transfer performance without impairing fluidity even for highly viscous liquids, and is used for cooling highly viscous or ultra-highly viscous liquids. It is important to contribute to the practical application of a plate heat exchanger that can be used for Moreover, since the temperature of the cooling water is raised without relying on a separate heat source, it is extremely advantageous from the viewpoint of cost and energy saving.

【図面の簡単な説明】[Brief description of drawings]

第1図はこの発明を実施するためのプレート式冷却装置
のフロシート、 第2図は伝熱板を介して隣り合った通路内における処理
液および冷却水の温度分布図である。 2:伝熱板 4:処理液通路 6:冷却水通路 8:プレート式熱交換器 18:循環通路 20:流量制御弁 22:サーモコントローラ
FIG. 1 is a flow sheet of a plate-type cooling device for carrying out the present invention, and FIG. 2 is a temperature distribution diagram of treatment liquid and cooling water in passages adjacent to each other via a heat transfer plate. 2: Heat transfer plate 4: Treatment liquid passage 6: Cooling water passage 8: Plate heat exchanger 18: Circulation passage 20: Flow control valve 22: Thermo controller

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】伝熱板を介して隣り合った通路にそれぞれ
流体を供給して両流体間で熱交換を行わせるに際し、一
方の通路に処理液を供給し、他方の通路に冷却水を供給
し、かつ、熱交換により昇温した冷却水の少なくとも一
部を再循環させることにより、通路内の冷却水温度を処
理液の粘度に見合った適当な値に調整するようにしたこ
とを特徴とする高粘度液の冷却方法。
1. When supplying fluid to adjacent passages via a heat transfer plate to cause heat exchange between the fluids, a treatment liquid is supplied to one passage and a cooling water is supplied to the other passage. It is characterized in that the temperature of the cooling water in the passage is adjusted to an appropriate value corresponding to the viscosity of the processing liquid by supplying and recirculating at least a part of the cooling water heated by heat exchange. Cooling method for high viscosity liquid.
JP1936387A 1987-01-28 1987-01-28 Cooling method for high viscosity liquid Expired - Fee Related JPH087031B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1936387A JPH087031B2 (en) 1987-01-28 1987-01-28 Cooling method for high viscosity liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1936387A JPH087031B2 (en) 1987-01-28 1987-01-28 Cooling method for high viscosity liquid

Publications (2)

Publication Number Publication Date
JPS63279099A JPS63279099A (en) 1988-11-16
JPH087031B2 true JPH087031B2 (en) 1996-01-29

Family

ID=11997280

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1936387A Expired - Fee Related JPH087031B2 (en) 1987-01-28 1987-01-28 Cooling method for high viscosity liquid

Country Status (1)

Country Link
JP (1) JPH087031B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103533838B (en) * 2011-03-17 2015-06-10 雀巢产品技术援助有限公司 Systems and methods for heat exchange

Also Published As

Publication number Publication date
JPS63279099A (en) 1988-11-16

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