JP5189932B2 - Variable baffle tray - Google Patents

Variable baffle tray Download PDF

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JP5189932B2
JP5189932B2 JP2008221493A JP2008221493A JP5189932B2 JP 5189932 B2 JP5189932 B2 JP 5189932B2 JP 2008221493 A JP2008221493 A JP 2008221493A JP 2008221493 A JP2008221493 A JP 2008221493A JP 5189932 B2 JP5189932 B2 JP 5189932B2
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perforated plate
tower
tray
plate
baffle
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JP2010051917A (en
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秀夫 野田
寛司 山路
晃 高石
伸行 倉谷
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Kansai Chemical Engineering Co Ltd
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Kansai Chemical Engineering Co Ltd
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Description

本発明は、蒸留塔、モロミ塔、吸収塔などの棚段塔に用いられるバッフルトレイに関する。   The present invention relates to a baffle tray used for a plate tower such as a distillation tower, a moromi tower, and an absorption tower.

蒸留塔、モロミ塔、吸収塔などの棚段塔の各段に備えられるトレイとして、シーブトレイ、リフトトレイ、バッフルトレイなどが挙げられる。   Examples of trays provided in each stage of a tower column such as a distillation tower, a moromi tower, and an absorption tower include a sieve tray, a lift tray, a baffle tray, and the like.

シーブトレイは、複数の孔が形成された多孔板からなり、形状がシンプルであるため、工業的に広く使われている。このシーブトレイは、様々な改良がなされている。   The sheave tray is composed of a perforated plate in which a plurality of holes are formed, and has a simple shape, so that it is widely used industrially. Various improvements have been made to the sheave tray.

例えば、特許文献1には、シーブトレイに衝撃または振動を与えて蒸留効率を改良することが記載されている。特許文献2には、固定多孔板と外力によって移動し得る可動多孔板とから構成されるシーブトレイが記載されている。特許文献2のシーブトレイは、多孔板の孔の面積(開孔比)を調整して溶媒の蒸気および液体の還流量、圧力などを適宜調整することができ、高いエネルギー効率で蒸留が行われ、省エネが可能となる。   For example, Patent Document 1 describes improving the distillation efficiency by applying an impact or vibration to the sieve tray. Patent Document 2 describes a sheave tray that includes a fixed perforated plate and a movable perforated plate that can be moved by an external force. The sieve tray of Patent Document 2 can adjust the area of the holes of the perforated plate (opening ratio) to appropriately adjust the solvent vapor and liquid reflux amount, pressure, etc., and distillation is performed with high energy efficiency. Energy saving is possible.

一方、リフトトレイは、各トレイが固定多孔板と可動多孔板との2枚の多孔板からなり、可動多孔板が、基本的に棚段塔内部の蒸気あるいは液体の流れに依存して、固定多孔板の上を浮遊するように構成されている。例えば、特許文献3に記載のリフトトレイは、蒸気あるいは液体の流れだけに依存して、可動多孔板が浮遊するのではなく、可動多孔板が外力によって可動し得るように構成されている。   On the other hand, the lift tray consists of two perforated plates, a fixed perforated plate and a movable perforated plate, and the movable perforated plate is basically fixed depending on the flow of vapor or liquid inside the plate tower. It is configured to float on the perforated plate. For example, the lift tray described in Patent Document 3 is configured so that the movable porous plate can be moved by an external force, not depending on only the flow of vapor or liquid, rather than the movable porous plate floating.

特許文献2および3に記載されるように、可動式のトレイは、一般的にチェンジトレイと称され、開孔比を調整し得るので、高いエネルギー効率で蒸留が行われ、省エネが可能となる。   As described in Patent Documents 2 and 3, the movable tray is generally referred to as a change tray, and can adjust the aperture ratio, so that distillation is performed with high energy efficiency and energy saving is possible. .

ところで、多孔板で構成されるシーブトレイおよびリフトトレイは、液体のみの原料を蒸留する場合には、上述のように高いエネルギー効率で蒸留が行われるなどの効果を発揮することができる。しかし、固形物、繊維状の物質などが混入しているスラリーなどを蒸留する場合、多孔板で構成されるシーブトレイおよびリフトトレイを用いた場合、以下のような問題を生じるおそれがある。   By the way, the sieve tray and lift tray formed of a perforated plate can exhibit effects such as distillation performed with high energy efficiency as described above when a liquid-only raw material is distilled. However, when distilling a slurry mixed with a solid substance, a fibrous substance, or the like, the following problems may occur when a sieve tray and a lift tray constituted by a perforated plate are used.

近年、トウモロコシ、稲わらなどを粉砕して発酵させた発酵物からエタノール(バイオエタノール)を回収する研究が進められている。このような発酵物には、原料の皮、未発酵のトウモロコシ、未発酵の稲わら、繊維状の物質などの発酵残渣、酵母などの固形の夾雑物が含まれている。このような発酵物を、多孔板で構成されるシーブトレイ、リフトトレイなどを備える蒸留塔を用いて、加熱してエタノールを回収する場合、夾雑物の飛散あるいは加熱による発酵物中の夾雑物の固形化などによりトレイに付着し、トレイに形成された孔を被覆するあるいは目詰まりを生じるおそれがある。一旦、孔への夾雑物もしくは固形物の付着または目詰まりが生じると、さらに夾雑物が付着して、付着物を成長させ、付着物がトレイ上に堆積、あるいは固定多孔板と可動多孔板との隙間を閉塞することになる(すなわち、蒸留塔内に詰まりが生じる)。   In recent years, research on recovering ethanol (bioethanol) from fermented material obtained by pulverizing and fermenting corn, rice straw, and the like has been underway. Such fermented products include raw leather, unfermented corn, unfermented rice straw, fermentation residues such as fibrous substances, and solid impurities such as yeast. When such a fermented product is heated to recover ethanol by using a distillation tower equipped with a sieve tray, a lift tray or the like composed of a perforated plate, the solids of the contaminant in the fermented product are scattered or heated. There is a risk that it will adhere to the tray due to the conversion, etc., covering the holes formed in the tray or clogging. Once the contaminants or solids adhere to the holes or become clogged, the foreign matter further adheres and grows, and the deposits accumulate on the tray, or the fixed perforated plate and the movable perforated plate (That is, clogging occurs in the distillation column).

このように、蒸留塔内に詰まりが生じると蒸留塔が運転不能となり、運転を停止して洗浄しなければならない。したがって、固形物、繊維状の物質などの夾雑物が混入しているスラリーを蒸留する場合、多孔板で構成されるシーブトレイおよびリフトトレイを用いると、これらのトレイの効果を発揮するどころか、かえって効率が悪くなる。   Thus, when clogging occurs in the distillation column, the distillation column becomes inoperable and must be stopped and washed. Therefore, when distilling slurries mixed with solids, fibrous substances, and other contaminants, the use of sieve trays and lift trays composed of perforated plates is more efficient than the effects of these trays. Becomes worse.

そこで、蒸留塔などの棚段塔に詰まりを生じさせにくいトレイとして、バッフルトレイが挙げられる。バッフルトレイは、図1(a)に示すように、例えば、円筒状の棚段塔11の内壁面および棚段塔11の中心部に、無孔質の板(無孔板12aおよび12b)が交互に段状に構成されたトレイである。棚段塔11の中心部に配置される無孔板12bは、支柱13などによって固定されている。また、図1(b)に示すように、例えば、半円形の無孔板12aが、棚段塔11の内壁面に、交互に段状に構成されたバッフルトレイもある。   Then, a baffle tray is mentioned as a tray which is hard to produce clogging in plate towers, such as a distillation tower. As shown in FIG. 1 (a), the baffle tray has, for example, non-porous plates (non-porous plates 12a and 12b) on the inner wall surface of the cylindrical plate tower 11 and the central portion of the plate tower 11. It is the tray comprised by the step shape alternately. The non-perforated plate 12b disposed at the center of the shelf tower 11 is fixed by a column 13 or the like. In addition, as shown in FIG. 1B, for example, there is a baffle tray in which semicircular non-perforated plates 12 a are alternately formed on the inner wall surface of the shelf tower 11.

バッフルトレイは、シーブトレイなどのように多孔板が用いられているわけではなく、無孔板が用いられているため、例えば、固形物、繊維状の物質などの夾雑物が混入しているスラリーなどの蒸留に用いたとしても、蒸留塔に詰まりを生じさせにくい。しかし、バッフルトレイは、シーブトレイおよびリフトトレイと比べて蒸留あるいは分留効率が悪く、さらにトレイの段数もシーブトレイなどと比べて多段にする必要があり、棚段塔を非常に高くしなければならないという問題がある。   The baffle tray is not a perforated plate like a sieve tray, but a non-porous plate is used. For example, a slurry mixed with impurities such as solids and fibrous substances, etc. Even if it is used for distillation, it is difficult to cause clogging in the distillation column. However, baffle trays are less efficient for distillation or fractionation than sieve trays and lift trays, and the number of trays must be multistage compared to sieve trays, etc., and the tower column must be very high. There's a problem.

そこで、固形物、繊維状の物質などの固形の夾雑物が混入しているスラリーであっても、効率よく蒸留あるいは分留処理し得るトレイが望まれている。
特開平5−115701号公報 特開2005−131586号公報 特開平5−115702号公報
Therefore, there is a demand for a tray that can be efficiently distilled or fractionated even in a slurry in which solid impurities such as solid substances and fibrous substances are mixed.
Japanese Patent Laid-Open No. 5-115701 JP 2005-131586 A JP-A-5-115702

本発明は、固形物、繊維状の物質などの固形の夾雑物が混入しているスラリーを、蒸留に供する場合であっても、効率よく処理することができ、安定して装置を運転し得るバッフルトレイを提供することを目的とする。   In the present invention, even when a slurry in which solid impurities such as solid substances and fibrous substances are mixed is subjected to distillation, the slurry can be efficiently processed and the apparatus can be operated stably. An object is to provide a baffle tray.

本発明は、バッフルトレイを提供し、該バッフルトレイは、棚段塔の内部に配置された第1の無孔板および第2の無孔板でなり、該第1の無孔板および該第2の無孔板は、いずれも該棚段塔の内壁面に配置され、かつ交互に段構造を構成するように配置されているか、あるいは該第1の無孔板は該棚段塔の内壁面に配置され、該第2の無孔板が該棚段塔の中心部に配置されており、そして該第1の無孔板および該第2の無孔板の少なくとも一方は、該棚段塔の上下方向に昇降し得るように構成されている。すなわち、本発明のバッフルトレイは、可変バッフルトレイである。   The present invention provides a baffle tray, and the baffle tray is composed of a first non-perforated plate and a second non-perforated plate arranged inside a tray tower, and the first non-perforated plate and the second non-perforated plate. Each of the two non-perforated plates is disposed on the inner wall surface of the plate tower and is alternately arranged to form a step structure, or the first non-perforated plate is disposed inside the plate tower. Disposed on the wall, the second non-perforated plate is disposed in the center of the shelf tower, and at least one of the first non-perforated plate and the second non-perforated plate It is configured to move up and down in the vertical direction of the tower. That is, the baffle tray of the present invention is a variable baffle tray.

1つの実施態様では、上記第1の無孔板または上記第2の無孔板は、該無孔板がそれぞれ独立して昇降し得るように構成されている。   In one embodiment, the first non-perforated plate or the second non-perforated plate is configured such that the non-perforated plate can be moved up and down independently.

1つの実施態様では、上記第1の無孔板は固定され、そして上記第2の無孔板は昇降し得るように構成されている。   In one embodiment, the first non-perforated plate is fixed, and the second non-perforated plate is configured to move up and down.

さらに、本発明は、上記バッフルトレイを備える棚段塔を提供する。   Furthermore, this invention provides a plate tower provided with the said baffle tray.

1つの実施態様では、上記棚段塔は、蒸留塔、モロミ塔、または吸収塔である。   In one embodiment, the plate tower is a distillation tower, a Moromi tower, or an absorption tower.

本発明によれば、固形物、繊維状の物質などの固形の夾雑物が混入しているスラリーを、蒸留などの精製処理に供する場合であっても、効率よく処理することができ、安定して装置を運転し得る。   According to the present invention, even when a slurry in which solid impurities such as a solid substance and a fibrous substance are mixed is subjected to a purification treatment such as distillation, the slurry can be efficiently treated and stabilized. Can operate the device.

本発明のバッフルトレイを、添付の図面を参照して説明する。   The baffle tray of the present invention will be described with reference to the accompanying drawings.

図2に、本発明のバッフルトレイの一実施態様を示す。図2に記載のバッフルトレイは、棚段塔21の内壁面に配置された第1の無孔板22aおよび棚段塔21の中心部に配置された第2の無孔板22bからなる。   FIG. 2 shows an embodiment of the baffle tray of the present invention. The baffle tray illustrated in FIG. 2 includes a first non-perforated plate 22 a disposed on the inner wall surface of the shelf tower 21 and a second non-perforated plate 22 b disposed at the center of the shelf tower 21.

第1の無孔板22aの形状は、設置される棚段塔の形状、大きさなどに合わせて適宜設定され得、第1の無孔板22aの中心部は、刳り貫かれた形状を有している。刳り貫かれた形状は、円形、多角形(例えば、三角形、四角形など)など特に限定されない。第2の無孔板22bの形状もまた、特に限定されず、第1の無孔板22aの中心部を刳り貫いた形状と同一でもよく、異なっていてもよく、好ましくは同一である。第1の無孔板22aと第2の無孔板22bとは嵌合するように、あるいは第2の無孔板22bが第1の無孔板22aの刳り貫かれた形状を覆うか、または刳り貫かれた形状より少し小さく隙間ができるように構成される。   The shape of the first non-perforated plate 22a can be appropriately set in accordance with the shape and size of the shelf tower to be installed, and the central portion of the first non-perforated plate 22a has a hollow shape. doing. The punched shape is not particularly limited, such as a circle or a polygon (for example, a triangle or a quadrangle). The shape of the second non-perforated plate 22b is also not particularly limited, and may be the same as or different from the shape of the first non-perforated plate 22a pierced through the center, and is preferably the same. The first non-perforated plate 22a and the second non-perforated plate 22b are fitted together, or the second non-perforated plate 22b covers the shape of the first non-perforated plate 22a, or It is configured to create a gap slightly smaller than the shape that has been punched.

図2(a)は、第2の無孔板22bを第1の無孔板22aと同一平面状に配置した状態を示す概略図であり、そして図2(b)は、第2の無孔板22bを上昇させた状態を示す概略図である。   FIG. 2A is a schematic view showing a state in which the second non-porous plate 22b is arranged on the same plane as the first non-porous plate 22a, and FIG. 2B is a second non-porous plate. It is the schematic which shows the state which raised the board 22b.

第1の無孔板22aは、棚段塔21の内壁面に固定されている。一方、第2の無孔板22bは、棚段塔21の中心部で支柱23に連結している。支柱23の先端は、梃子棒24の一端と連結している。梃子棒24の他端は、棚段塔21の外部に突出している。この梃子棒24を操作することによって、第2の無孔板22bは、昇降され得る。   The first non-porous plate 22 a is fixed to the inner wall surface of the shelf tower 21. On the other hand, the second non-perforated plate 22 b is connected to the column 23 at the center of the shelf tower 21. The front end of the column 23 is connected to one end of the lever rod 24. The other end of the insulator rod 24 protrudes outside the shelf tower 21. By operating this lever rod 24, the second non-perforated plate 22b can be raised and lowered.

第1の無孔板22aと第2の無孔板22bとの段差(ΔH)の最大値は、棚段塔21の内径、棚段塔21の高さ、設置されているバッフルトレイの枚数、第2の無孔板22bの大きさなどによって適宜設定され得る。好ましくは、段差(ΔH)は、最大で棚間隔の半分であり得、より好ましくは最大で約20cmであり得る。   The maximum value of the step (ΔH) between the first non-porous plate 22a and the second non-porous plate 22b is the inner diameter of the plate tower 21, the height of the plate tower 21, the number of baffle trays installed, It can be set as appropriate depending on the size of the second non-perforated plate 22b. Preferably, the step (ΔH) can be at most half the shelf spacing, more preferably at most about 20 cm.

図2のバッフルトレイは、梃子棒24の操作によって第2の無孔板22bを昇降し得るが、第2の無孔板22bの昇降手段は、この手段に限定されない。例えば、アクチュエーターなどを搭載し、電気的制御によって昇降させ得る手段であってもよく、センサーなどを搭載し、棚段塔21内の圧力、温度などのデータを予めプログラミングしておき、自動的に昇降させ得る手段であってもよい。   The baffle tray of FIG. 2 can move the second non-perforated plate 22b up and down by operating the lever rod 24, but the elevating means of the second non-perforated plate 22b is not limited to this means. For example, it may be a means that is equipped with an actuator and can be moved up and down by electrical control, is equipped with a sensor and the like, and data such as pressure and temperature in the shelf tower 21 is programmed in advance and automatically It may be a means that can be moved up and down.

上記のように、図2のバッフルトレイは、第1の無孔板22aが棚段塔21の内壁面に固定され、棚段塔21の中心部に配置された第2の無孔板22bを昇降し得る構造を有する。しかし、本発明のバッフルトレイは、第2の無孔板22bが固定され、棚段塔21の内壁面に配置された第1の無孔板22aが昇降し得る構造であってもよく、第1の無孔板22aおよび第2の無孔板22bの両方を昇降し得る構造であってもよい。   As described above, the baffle tray shown in FIG. 2 has the first non-perforated plate 22 a fixed to the inner wall surface of the shelf tower 21 and the second non-perforated plate 22 b arranged at the center of the shelf tower 21. It has a structure that can move up and down. However, the baffle tray of the present invention may have a structure in which the second non-perforated plate 22b is fixed, and the first non-perforated plate 22a disposed on the inner wall surface of the shelf tower 21 can move up and down. The structure which can raise / lower both the 1 non-porous board 22a and the 2nd non-porous board 22b may be sufficient.

棚段塔21の内壁面に配置された第1の無孔板22aを昇降し得る構成とする場合、昇降機構が複雑になる。したがって、簡単な機構で昇降可能な点で、第1の無孔板22aを棚段塔21の内壁面に固定し、棚段塔21の中心部に配置された第2の無孔板22bを昇降し得る構造を有することが好ましい。   When it is set as the structure which can raise / lower the 1st non-perforated board 22a arrange | positioned at the inner wall face of the plate tower 21, the raising / lowering mechanism becomes complicated. Accordingly, the first non-perforated plate 22a is fixed to the inner wall surface of the shelf tower 21 and the second non-perforated plate 22b disposed at the center of the shelf tower 21 is provided so that it can be moved up and down with a simple mechanism. It is preferable to have a structure that can move up and down.

さらに、第2の無孔板の形状は平板ではなくてもよい。例えば、図3に示すバッフルトレイを構成する第2の無孔板32bのように、湾曲した無孔板でもよい。図3のバッフルトレイのように、湾曲した第2の無孔板32bを使用すると、平板の場合よりもバッフルトレイの強度が増す。したがって、大型の棚段塔であっても、安定した強度を確保し得る。   Furthermore, the shape of the second non-perforated plate may not be a flat plate. For example, a curved non-perforated plate may be used like the second non-perforated plate 32b constituting the baffle tray shown in FIG. When the curved second non-perforated plate 32b is used as in the baffle tray of FIG. 3, the strength of the baffle tray is increased as compared with the case of a flat plate. Therefore, even if it is a large-sized tray tower, the stable intensity | strength can be ensured.

図4に、本発明のバッフルトレイの別の実施態様を示す。図4のバッフルトレイは、第1の無孔板42aおよび第2の無孔板42bが、いずれも棚段塔41の内壁面に配置され、かつ交互に段構造を構成するように配置されている。   FIG. 4 shows another embodiment of the baffle tray of the present invention. In the baffle tray of FIG. 4, the first non-perforated plate 42 a and the second non-perforated plate 42 b are both arranged on the inner wall surface of the shelf tower 41 and alternately arranged in a step structure. Yes.

第1の無孔板42aは、棚段塔41の内壁面に固定されている。一方、第2の無孔板42bは、棚段塔41の内壁面に固定されておらず支柱43に連結しており、棚段塔41の内壁面に沿って上下方向に沿って摺動可能に配置されている。支柱43の先端は、梃子棒44の一端と連結している。梃子棒44の他端は、棚段塔41の外部に突出している。この梃子棒44を操作することによって、第2の無孔板42bは、昇降され得る。   The first non-perforated plate 42 a is fixed to the inner wall surface of the shelf tower 41. On the other hand, the second non-perforated plate 42 b is not fixed to the inner wall surface of the shelf tower 41 and is connected to the column 43, and can slide along the inner wall surface of the shelf tower 41 in the vertical direction. Is arranged. The tip end of the column 43 is connected to one end of the lever rod 44. The other end of the insulator rod 44 protrudes outside the shelf tower 41. By operating this lever rod 44, the second non-perforated plate 42b can be moved up and down.

図5に、本発明のバッフルトレイのさらに別の実施態様を示す。図2のバッフルトレイは、1本の支柱23に全ての第2の無孔板22bを連結させた構造を有する実施態様であるのに対し、図5のバッフルトレイは、複数の支柱53を有し、各支柱53に1枚の第2の無孔板52bを連結させた構造を有する。すなわち、図5に示すバッフルトレイは、第2の無孔板52bがそれぞれ独立して(すなわち、1枚の第2の無孔板52bごとに)、昇降可能な構造を有している。   FIG. 5 shows still another embodiment of the baffle tray of the present invention. The baffle tray of FIG. 2 is an embodiment having a structure in which all the second non-perforated plates 22 b are connected to one column 23, whereas the baffle tray of FIG. 5 has a plurality of columns 53. Each strut 53 has a structure in which one second non-porous plate 52b is connected. That is, the baffle tray shown in FIG. 5 has a structure in which the second non-perforated plate 52b can be moved up and down independently (that is, for each second non-perforated plate 52b).

このような構造を有することによって、より緻密な圧力調整が可能となる。例えば、図5(a)に示すように、棚段塔51の最上部のバッフルトレイで仕切られた上下の空間において、圧力差ΔP1が異常に大きくなった場合、棚段塔51の最上部のバッフルトレイを構成する第2の無孔板52bのみを上昇させることによって、圧力差ΔP1が異常に大きくなった部分のみの蒸気または液体の流量を調整して圧力を調整し得る(図5(b))。そのため、棚段塔51の底部などその他の部分の蒸気または液体の流量は、ほとんど変化しないので、より効率よく蒸留、分留などの精製処理を行い得る。   By having such a structure, more precise pressure adjustment is possible. For example, as shown in FIG. 5A, in the upper and lower spaces partitioned by the uppermost baffle tray of the plate tower 51, when the pressure difference ΔP1 becomes abnormally large, By raising only the second non-perforated plate 52b constituting the baffle tray, the pressure can be adjusted by adjusting the flow rate of the vapor or liquid only in the portion where the pressure difference ΔP1 becomes abnormally large (FIG. 5B). )). For this reason, the flow rate of the vapor or liquid in other parts such as the bottom of the plate column 51 hardly changes, so that purification treatment such as distillation and fractional distillation can be performed more efficiently.

図5に示すバッフルトレイは、それぞれの第2の無孔板52bが梃子棒54a〜54cの操作によって昇降され得る構造を有するが、上記のように、それぞれの第2の無孔板52bの昇降を、電気的制御で行ってもよく、プログラミング制御で自動的に行ってもよい。   The baffle tray shown in FIG. 5 has a structure in which each second non-perforated plate 52b can be raised and lowered by operating the lever bars 54a to 54c. As described above, the second non-perforated plate 52b is raised and lowered. May be performed by electrical control or automatically by programming control.

さらに、第2の無孔板52bを固定し、棚段塔51の内壁面に配置された第1の無孔板52aを、各第1の無孔板52aが棚段塔51の内壁面に沿って昇降し得る構造を有していてもよく、あるいは各第1の無孔板52aおよび各第2の無孔板52bが昇降し得る構造を有していてもよい。   Further, the second non-perforated plate 52b is fixed, and the first non-perforated plate 52a disposed on the inner wall surface of the shelf tower 51 is connected to the first non-perforated plate 52a on the inner wall surface of the shelf tower 51. You may have the structure which can be raised / lowered along, or may have the structure which each 1st non-perforated plate 52a and each 2nd non-perforated plate 52b can raise / lower.

図5のバッフルトレイは、各第2の無孔板52bが、それぞれ独立して昇降可能な構造を有しているが、例えば、所望の枚数(例えば、2枚〜4枚)の第2の無孔板52bを、一緒に昇降し得る構造であってもよい。   The baffle tray of FIG. 5 has a structure in which each second non-perforated plate 52b can be moved up and down independently. For example, a desired number (for example, 2 to 4) of second plates can be used. The structure which can raise / lower the non-perforated plate 52b together may be sufficient.

次いで、本発明のバッフルトレイを内部熱交換型蒸留塔(HIDiC)に用いた場合の一実施態様を説明する。   Next, an embodiment when the baffle tray of the present invention is used in an internal heat exchange distillation column (HIDiC) will be described.

図6に示す内部熱交換型蒸留塔61は、2重円筒型構造を有し、外筒66のトレイとして、本発明のバッフルトレイを使用している。すなわち、外筒66の内壁面に第1の無孔板62aが固定され、第2の無孔板62bは、支柱63に連結しており、外筒66の中心部(内筒67の外壁面)に、内筒67の外壁面に沿って上下方向に摺動可能に配置されている。支柱63の先端は、梃子棒64の一端と連結している。梃子棒64の他端は、棚段塔61の外部に突出している。この梃子棒64を操作することによって、第2の無孔板62bは、内筒67の外壁面に沿って昇降され得る。   The internal heat exchange distillation column 61 shown in FIG. 6 has a double cylindrical structure, and uses the baffle tray of the present invention as the tray of the outer cylinder 66. That is, the first non-perforated plate 62 a is fixed to the inner wall surface of the outer cylinder 66, and the second non-perforated plate 62 b is connected to the column 63, and the central portion of the outer cylinder 66 (the outer wall surface of the inner cylinder 67 ) Is slidable in the vertical direction along the outer wall surface of the inner cylinder 67. The tip of the column 63 is connected to one end of the lever rod 64. The other end of the insulator rod 64 protrudes outside the shelf tower 61. By operating the lever rod 64, the second non-hole plate 62 b can be lifted and lowered along the outer wall surface of the inner cylinder 67.

図6に示すような内部熱交換型蒸留塔61に、本発明のバッフルトレイを用いると、第2の無孔板62bが、内筒67の外壁面を上下方向に摺動するため、内筒67の外壁面に付着している固形物などを除去することも可能であり、熱効率が低下することなく蒸留し得る。   When the baffle tray of the present invention is used for the internal heat exchange distillation column 61 as shown in FIG. 6, the second non-perforated plate 62b slides on the outer wall surface of the inner cylinder 67 in the vertical direction. It is also possible to remove solid matter and the like adhering to the outer wall surface 67, and distillation can be performed without lowering the thermal efficiency.

このように、本発明のバッフルトレイは、可変型のバッフルトレイであり、第1の無孔板と第2の無孔板との段差(隙間)を調節することによって、蒸気または液体の流量を調整して圧力調整が可能となる。したがって、本発明のバッフルトレイは、バッフルトレイが本来有する詰まりを生じさせにくいという特徴を生かしながら、効率よく蒸留などの精製処理を行うことを可能とする。本発明の可変バッフルトレイは、蒸留塔、モロミ塔、吸収塔などの棚段塔に備えられる。   Thus, the baffle tray of the present invention is a variable baffle tray, and the flow rate of vapor or liquid is adjusted by adjusting the step (gap) between the first non-porous plate and the second non-porous plate. The pressure can be adjusted by adjusting. Therefore, the baffle tray of the present invention makes it possible to efficiently perform a purification process such as distillation while taking advantage of the feature that the baffle tray does not easily cause clogging. The variable baffle tray of the present invention is provided in a plate tower such as a distillation tower, a moromi tower, or an absorption tower.

(実施例1)
図7に示す圧力損失を測定し得る実験装置を用いて、本発明の可変バッフルトレイを用いた棚段塔の水−空気の系における運転状況を確認した。
Example 1
Using the experimental apparatus capable of measuring the pressure loss shown in FIG. 7, the operating condition in the water-air system of the plate tower using the variable baffle tray of the present invention was confirmed.

まず、棚段塔111に、ガス送風機115、液循環ポンプ116、圧力損失測定マノメーター117、液流量計118、およびガス速度計119を、図7に示すように接続した。棚段塔111は、内径200mmの円筒形であり、内部に第1の無孔板112aおよび第2の無孔板112bでなる本発明のバッフルトレイを1段備えた。第2の無孔板112bは、直径100mmの円形であり(すなわち、第1の無孔板112aは、中心部が直径100mmの円形に刳り貫かれている)、支柱113に連結され梃子棒114で昇降し得るように構成されている。   First, a gas blower 115, a liquid circulation pump 116, a pressure loss measurement manometer 117, a liquid flow meter 118, and a gas velocity meter 119 were connected to the plate tower 111 as shown in FIG. The shelf tower 111 has a cylindrical shape with an inner diameter of 200 mm, and includes one stage of the baffle tray of the present invention including the first non-perforated plate 112a and the second non-perforated plate 112b. The second non-perforated plate 112b has a circular shape with a diameter of 100 mm (that is, the first non-perforated plate 112a has a central portion penetrated into a circular shape with a diameter of 100 mm) and is connected to the support column 113 and the lever rod 114. It can be moved up and down.

次いで、棚段塔111にガス送風機115を用いて空気を送り込み、液循環ポンプ116を用いて、図7中の矢印の方向に水を循環させた。水は、200L/分/mの割合で循環させた。 Subsequently, air was sent into the plate tower 111 using the gas blower 115, and water was circulated in the direction of the arrow in FIG. Water was circulated at a rate of 200 L / min / m 2 .

第1の無孔板112aおよび第2の無孔板112bの間隔を4mm〜10mmの間で一定の間隔とした場合において、空気量(風速)を変化させたときの圧力損失を図8に示す。さらに、空気量を一定(0.7m/秒)にした場合の第1の無孔板112aおよび第2の無孔板112bの間隔を変化させたときの圧力損失を図9に示す。   FIG. 8 shows the pressure loss when the air amount (wind speed) is changed when the interval between the first non-porous plate 112a and the second non-porous plate 112b is a constant interval between 4 mm and 10 mm. . Further, FIG. 9 shows pressure loss when the distance between the first non-porous plate 112a and the second non-porous plate 112b is changed when the air amount is constant (0.7 m / sec).

図8および図9に示すように、棚段塔111は、バッフルトレイの間隔を数ミリ単位で制御して、圧力損失を棚段塔の外部から細かく制御し得る。したがって、詰まりなどにより棚段塔の内部の圧力が上昇しても、棚段塔の外部からバッフルトレイの間隔を調整する(トレイ間の間隔を広げる)ことで、一定の圧力損失を維持し得、蒸留などの精製処理を継続して行い得る。   As shown in FIGS. 8 and 9, the plate tower 111 can finely control the pressure loss from the outside of the plate tower by controlling the interval between the baffle trays in units of several millimeters. Therefore, even if the pressure inside the plate tower rises due to clogging, etc., a constant pressure loss can be maintained by adjusting the interval between the baffle trays from the outside of the plate tower (widening the space between the trays). Further, a purification treatment such as distillation can be continued.

本発明によれば、発酵残渣、繊維状の物質などの固形の夾雑物が混入しているスラリーを、蒸留などの精製処理に供する場合であっても、効率よく処理することができ、安定して装置を運転し得る。したがって、発酵残渣、繊維状の物質などの固形の夾雑物が混入しているスラリー、例えば、バイオエタノールの蒸留などに有用である。   According to the present invention, even when a slurry in which solid impurities such as fermentation residues and fibrous substances are mixed is subjected to a purification treatment such as distillation, the slurry can be efficiently treated and stabilized. Can operate the device. Therefore, it is useful for a slurry in which solid impurities such as fermentation residues and fibrous substances are mixed, for example, bioethanol distillation.

一般的なバッフルトレイを示す概略図である。It is the schematic which shows a general baffle tray. 本発明のバッフルトレイの一実施態様を示す概略図である。It is the schematic which shows one embodiment of the baffle tray of this invention. 本発明のバッフルトレイの他の実施態様を示す概略図である。It is the schematic which shows the other embodiment of the baffle tray of this invention. 本発明のバッフルトレイの別の実施態様を示す概略図である。It is the schematic which shows another embodiment of the baffle tray of this invention. 本発明のバッフルトレイのさらに別の実施態様を示す概略図であり、図5(b)は、第2の無孔板を上昇させて最上部のバッフルトレイの第1の無孔板と第2の無孔板との段差(隙間)を広げた場合を示す概略図である。FIG. 5B is a schematic view showing still another embodiment of the baffle tray of the present invention, and FIG. 5B is a diagram illustrating a first non-perforated plate and a second non-perforated plate of the uppermost baffle tray by raising the second non-perforated plate. It is the schematic which shows the case where the level | step difference (gap) with a non-perforated board is expanded. 本発明のバッフルトレイを内部熱交換型蒸留塔に用いた場合の一実施態様を示す概略図である。It is the schematic which shows one embodiment at the time of using the baffle tray of this invention for an internal heat exchange type | mold distillation column. 実施例1で用いたバッフルトレイの構造を示す模式図である。4 is a schematic diagram illustrating a structure of a baffle tray used in Example 1. FIG. 第1の無孔板および第2の無孔板の間隔を4mm〜10mmの間で一定の間隔とした場合において、空気量(風速)を変化させたときの圧力損失を示すグラフである。It is a graph which shows a pressure loss when changing the air quantity (wind speed) when the space | interval of a 1st non-perforated plate and a 2nd non-perforated plate is made into a fixed space | interval between 4 mm-10 mm. 空気量(風速)が一定の場合(0.7m/秒)における、第1の無孔板および第2の無孔板の間隔を変化させた場合の圧力損失を示すグラフである。It is a graph which shows the pressure loss at the time of changing the space | interval of a 1st non-perforated board and a 2nd non-perforated board in case air quantity (wind speed) is constant (0.7 m / sec).

符号の説明Explanation of symbols

11、21、31、41、51 棚段塔
12a、12b 無孔板
13、23、33、43、53、63 支柱
22a、32a、42a、52a、62a 第1の無孔板
22b、32b、42b、52b、62b 第2の無孔板
24、34、44、54、64 梃子棒
61 内部熱交換型蒸留塔
65 内筒のトレイ
66 外筒
67 内筒
111 棚段塔
112a 第1の無孔板
112b 第2の無孔板
113 支柱
114 梃子棒
115 ガス送風機
116 液循環ポンプ
117 圧力損失測定マノメーター
118 液流量計
119 ガス速度計
11, 21, 31, 41, 51 Shelf tower 12a, 12b Non-perforated plate 13, 23, 33, 43, 53, 63 Prop 22a, 32a, 42a, 52a, 62a First non-perforated plate 22b, 32b, 42b 52b, 62b Second non-perforated plate 24, 34, 44, 54, 64 Insulator rod 61 Internal heat exchange distillation column 65 Inner cylinder tray 66 Outer cylinder 67 Inner cylinder 111 Shelf tower 112a First non-perforated plate 112b 2nd non-perforated plate 113 support | pillar 114 insulator rod 115 gas blower 116 liquid circulation pump 117 pressure loss measurement manometer 118 liquid flow meter 119 gas velocimeter

Claims (5)

バッフルトレイであって、
棚段塔の内部に配置された第1の無孔板および第2の無孔板でなり、
該第1の無孔板および該第2の無孔板が、いずれも該棚段塔の内壁面に配置され、かつ交互に段構造を構成するように配置されているか、あるいは該第1の無孔板が該棚段塔の内壁面に配置され、該第2の無孔板が該棚段塔の中心部に配置されており、そして
該第1の無孔板および該第2の無孔板の少なくとも一方が、外力によって該棚段塔の上下方向に昇降し得るように構成されている、バッフルトレイ。
A baffle tray,
A first non-perforated plate and a second non-perforated plate disposed inside the plate tower,
The first non-perforated plate and the second non-perforated plate are both arranged on the inner wall surface of the shelf tower and alternately arranged in a step structure, or the first non-perforated plate A non-perforated plate is disposed on the inner wall surface of the tray tower, the second non-perforated plate is disposed in the center of the shelf tower, and the first non-perforated plate and the second non-perforated plate A baffle tray configured such that at least one of the perforated plates can be moved up and down in the vertical direction of the shelf tower by an external force .
前記第1の無孔板または前記第2の無孔板が、該無孔板がそれぞれ独立して昇降し得るように構成されている、請求項1に記載のバッフルトレイ。   2. The baffle tray according to claim 1, wherein the first non-perforated plate or the second non-perforated plate is configured such that the non-perforated plate can be moved up and down independently. 前記第1の無孔板が固定され、そして前記第2の無孔板が昇降し得るように構成されている、請求項1または2に記載のバッフルトレイ。   The baffle tray according to claim 1 or 2, wherein the first non-perforated plate is fixed and the second non-perforated plate can be moved up and down. 請求項1から3のいずれかの項に記載のバッフルトレイを備える、棚段塔。   A tray tower comprising the baffle tray according to any one of claims 1 to 3. 蒸留塔、モロミ塔、または吸収塔である、請求項4に記載の棚段塔。   The plate tower according to claim 4, which is a distillation tower, a moromi tower, or an absorption tower.
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