JP2011245410A - Device and method for supplying pressurized container - Google Patents

Device and method for supplying pressurized container Download PDF

Info

Publication number
JP2011245410A
JP2011245410A JP2010120299A JP2010120299A JP2011245410A JP 2011245410 A JP2011245410 A JP 2011245410A JP 2010120299 A JP2010120299 A JP 2010120299A JP 2010120299 A JP2010120299 A JP 2010120299A JP 2011245410 A JP2011245410 A JP 2011245410A
Authority
JP
Japan
Prior art keywords
back pressure
pressure valve
intermediate state
pressurized container
raw material
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.)
Granted
Application number
JP2010120299A
Other languages
Japanese (ja)
Other versions
JP5425706B2 (en
Inventor
Tomomoto Hayakawa
智基 早川
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.)
Tsukishima Kikai Co Ltd
Original Assignee
Tsukishima Kikai Co 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 Tsukishima Kikai Co Ltd filed Critical Tsukishima Kikai Co Ltd
Priority to JP2010120299A priority Critical patent/JP5425706B2/en
Publication of JP2011245410A publication Critical patent/JP2011245410A/en
Application granted granted Critical
Publication of JP5425706B2 publication Critical patent/JP5425706B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/78Recycling of wood or furniture waste

Landscapes

  • Screw Conveyors (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
  • Processing Of Solid Wastes (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent incorrect detection of formation of a filled object, increase in power requirement, and a blockage.SOLUTION: The problem is solved by a pressurized container supplying device 30 including: a material sealing feeder which continuously supplies a solid-liquid mixture material to a pressurized container 4 through a supplying pipe 32 while forming a filled object P formed by airtightly filling the material to the supplying pipe 32 to shield the upstream pressure of the supplying pipe 32 from the downstream pressure with the filled object P; a back pressure valve 40 disposed on the downstream side in the filled area 32z of the filled object P in the supplying pipe 32 of the feeder; a cylinder 42 of the back pressure valve 40; an intermediate state detecting device which detects whether a valve member 41 of the back pressure valve 40 is in an intermediate state between closed state and open state; a controller which controls the cylinder 42 to open the back pressure valve 40 when the intermediate state detecting device detects that the valve member 41 of the back pressure valve 40 is in the intermediate state.

Description

本発明は、液分及び固形分からなる固液混合原料を加圧容器器内へ連続供給するマテリアルシールタイプのフィーダーを採用した、加圧容器供給技術に関するものであり、特に木質バイオマスの加水分解反応における加圧反応容器への応用に好適な加圧容器供給技術に関するものである。   The present invention relates to a pressurized container supply technology that employs a material seal type feeder that continuously supplies a solid-liquid mixed raw material consisting of liquid and solid contents into a pressurized container, and in particular, hydrolysis reaction of woody biomass The present invention relates to a pressurized container supply technique suitable for application to a pressurized reaction container.

固形物と水との混合物や、高濃度スラリー等、液分及び固形分からなる固液混合原料を反応器に連続的に供給する場合、一般に、一軸ネジ式ポンプやスクリューフィーダー、ピストンフィーダーなどの押し込み型フィーダーが使用される。特に、加圧下の反応器に対するフィーダーは、反応器内圧をシールしつつ原料を押し込むことが要求される。このような要求を満たすフィーダーとして、原料を供給通路内に通過させながら圧縮して原料の充填体を形成し、この充填体(プラグ)によりその上流側と下流側とを遮断しつつ押し込む、いわゆるマテリアルシール型スクリューフィーダーや、ピストンフィーダーがある。以下、これらを総称してマテリアルシール型フィーダーという。
このようなマテリアルシール型フィーダーにおいては、原料供給開始時に上流側圧力と下流側圧力とを遮断しつつ充填体の形成を促すために、充填体の充填領域の下流側に隣接して背圧弁を設け、充填体が形成され次第背圧弁を開け、後は充填体を下流側から順に加圧容器に供給する一方で上流側に原料を補給して充填体を維持する、といった方法が一般的となっている。また、この際、充填体が形成されたか否かは、原料供給の摩擦抵抗の指標(例えば、供給機の電流値やスラスト力)を検出して判断することが一般的であった。
When continuously supplying a solid-liquid mixed material consisting of liquid and solid content such as a mixture of solid and water, high-concentration slurry, etc., to a reactor, in general, pushing in a single screw pump, screw feeder, piston feeder, etc. A mold feeder is used. In particular, the feeder for the reactor under pressure is required to push the raw material while sealing the reactor internal pressure. As a feeder satisfying such requirements, the raw material is compressed while passing through the supply passage to form a raw material filling body, and this filler (plug) is pushed in while blocking its upstream side and downstream side. There are material seal type screw feeders and piston feeders. Hereinafter, these are collectively referred to as a material seal type feeder.
In such a material seal type feeder, a back pressure valve is provided adjacent to the downstream side of the filling region of the filling body in order to promote the formation of the filling body while shutting off the upstream side pressure and the downstream side pressure at the start of raw material supply. As soon as the filling body is formed, the back pressure valve is opened, and after that, the filling body is supplied to the pressure vessel in order from the downstream side, while the raw material is replenished upstream to maintain the filling body. It has become. Further, at this time, it is common to determine whether or not the filler is formed by detecting an index of frictional resistance of the raw material supply (for example, a current value or a thrust force of the feeder).

特表昭57−500091号公報JP-T57-500091 特開2004−89016号公報JP 2004-89016 A 特開2004−337099号公報JP 2004-337099 A 特開平6−109227号公報JP-A-6-109227 特開平9−183516号公報JP-A-9-183516 特開2007−211096号公報JP 2007-211096 A 特開2006−068606号公報JP 2006-068606 A 特開2006−281037号公報JP 2006-281037 A 特開2004−121055号公報JP 2004-121055 A

しかし、従来の充填検出は、原料の性状が変化した場合や機械の摩耗が進行する等、シール部の形成に関係無く原料供給の摩擦抵抗が変化した場合に誤検出するおそれがあった。
また、従来の充填検出は、原料供給の摩擦抵抗という間接的な指標に基づくものであったため、充填体形成に対する反応が遅くなり、充填体及び背圧弁の両方が原料供給負荷となる状態が不必要に続くため、所要動力が増加し、充填体が供給管路内に閉塞するおそれもあった。
そこで、本発明の主たる課題は、充填体形成の誤検出、所要動力増、及び閉塞を防止することにある。
However, the conventional filling detection may be erroneously detected when the frictional resistance of the raw material supply changes regardless of the formation of the seal portion, such as when the properties of the raw material change or the wear of the machine progresses.
In addition, since the conventional filling detection is based on an indirect index of friction resistance of the raw material supply, the reaction to the formation of the filling body becomes slow, and the state in which both the filling body and the back pressure valve become the raw material supply load is unsatisfactory. Since it continued to be necessary, the required power increased, and there was also a risk that the filler was blocked in the supply pipe line.
Therefore, a main problem of the present invention is to prevent erroneous detection of formation of a filling body, increase in required power, and blockage.

上記課題を解決した本発明は次記のとおりである。
<請求項1記載の発明>
固液混合原料を、供給管路を介して加圧容器内へ連続供給するとともに、この供給管路に前記原料を気密充填してなる充填体を形成し、この充填体により供給管路の上流側圧力と下流側圧力とを遮断しつつ前記原料の供給を行う、マテリアルシール型フィーダーと、
このフィーダーの供給管路における前記充填体の充填領域の下流側に設けられた背圧弁と、
この背圧弁の開閉駆動装置と、
を備えた加圧容器供給装置であって、
前記背圧弁の弁体が閉状態と開状態との間の中間状態にあるか否かを検出する中間状態検出手段と、
この中間状態検出手段により前記背圧弁の弁体が前記中間状態にあることが検出されたときに前記開閉駆動装置により前記背圧弁を開ける制御を行う制御装置と、
を備えたことを特徴とする加圧容器供給装置。
The present invention that has solved the above problems is as follows.
<Invention of Claim 1>
The solid-liquid mixed raw material is continuously supplied into the pressurized container through the supply pipe, and a filling body is formed by hermetically filling the raw material in the supply pipe, and this filling body forms an upstream of the supply pipe. A material seal type feeder that supplies the raw material while blocking the side pressure and the downstream pressure,
A back pressure valve provided on the downstream side of the filling region of the filler in the feeder supply line;
An opening / closing drive for the back pressure valve;
A pressurized container supply device comprising:
Intermediate state detection means for detecting whether or not the valve body of the back pressure valve is in an intermediate state between a closed state and an open state;
A control device for performing control to open the back pressure valve by the opening / closing drive device when it is detected by the intermediate state detection means that the valve body of the back pressure valve is in the intermediate state;
A pressurized container supply device comprising:

(作用効果)
このようなマテリアルシール型フィーダーに背圧弁を設けた供給装置においては、原料の充填体が形成されると、背圧弁の弁体が原料の充填体により押し開けられる。よって、背圧弁の弁体が閉状態と開状態との間の中間状態にあるか否かを検出する中間状態検出手段を設けることにより、原料供給の摩擦抵抗に関係なく、しかも直接的に反応良く充填体の形成を検出できる。よって、充填体形成の誤検出、所要動力増、及び閉塞を防止できるようになる。
(Function and effect)
In a supply device in which such a material seal type feeder is provided with a back pressure valve, when the raw material filling body is formed, the valve body of the back pressure valve is pushed open by the raw material filling body. Therefore, by providing an intermediate state detection means for detecting whether or not the valve body of the back pressure valve is in the intermediate state between the closed state and the open state, the reaction can be performed directly regardless of the friction resistance of the raw material supply. The formation of the filler can be detected well. Therefore, it is possible to prevent erroneous detection of the filling body formation, increase in required power, and blockage.

<請求項2記載の発明>
前記中間状態検出手段は、前記背圧弁の弁体の移動力により、前記背圧弁の弁体が前記閉状態にあるときと前記中間状態にあるときとでオン/オフが切り替わる閉リミットスイッチである、請求項1記載の加圧容器供給装置。
<Invention of Claim 2>
The intermediate state detection means is a closed limit switch that is turned on / off depending on the moving force of the valve body of the back pressure valve when the valve body of the back pressure valve is in the closed state and when in the intermediate state. The pressurized container supply device according to claim 1.

(作用効果)
このようなリミットスイッチを用いた中間状態検出手段は、簡素な装置構成で実施でき、検出も直接且つ確実であるため好ましい。
(Function and effect)
Such an intermediate state detecting means using a limit switch is preferable because it can be implemented with a simple device configuration and is directly and reliably detected.

<請求項3記載の発明>
前記フィーダーは、前記充填体の充填領域に向かって次第に内径が減少するように構成された前記供給管路と、この供給管路内に管軸方向に沿って設置されたスクリューと、このスクリューを回転駆動する電動機とを備えたプラグスクリューフィーダーであり、
前記中間状態検出手段に加えて、次の(イ)〜(ハ)の少なくとも一つの補助検出手段を備えており、
(イ)前記スクリュー軸のトルクを検出するトルク検出器、
(ロ)前記スクリュー軸のスラスト力を検出するスラスト力検出器、
(ハ)前記電動機の電流を検出する電流検出器、
前記制御装置は、補助検出手段による検出値が所定値以上であって、なおかつ前記中間状態検出手段により前記背圧弁の弁体が前記中間状態にあることが検出されたときに前記開閉駆動装置により前記背圧弁を開ける制御を行うものである、
請求項1又は2記載の加圧容器供給装置。
<Invention of Claim 3>
The feeder includes the supply pipe configured so that the inner diameter gradually decreases toward the filling region of the filler, a screw installed in the supply pipe along the pipe axis direction, and the screw. A plug screw feeder equipped with an electric motor for rotational driving,
In addition to the intermediate state detection means, it comprises at least one auxiliary detection means of the following (A) to (C):
(A) a torque detector for detecting the torque of the screw shaft;
(B) a thrust force detector for detecting a thrust force of the screw shaft;
(C) a current detector for detecting the current of the motor;
When the detected value by the auxiliary detecting means is equal to or greater than a predetermined value and the intermediate state detecting means detects that the valve body of the back pressure valve is in the intermediate state, the control device uses the opening / closing drive device. Control to open the back pressure valve,
The pressurized container supply apparatus according to claim 1 or 2.

(作用効果)
マテリアルシール型フィーダーとしては、電動機を駆動源とするスクリューフィーダーが好適である。このようなスクリューフィーダーでは、原料供給の摩擦抵抗と、スクリュー軸のトルク、スラスト力または電動機の電流とは相関関係を有し、原料充填体の形成と原料供給の摩擦抵抗とは相関関係を有する。つまり、スクリュー軸のトルク、スラスト力または電動機の電流と原料充填体の形成とは相関関係を有する。したがって、マテリアルシール型スクリューフィーダーを用いる場合、スクリュー軸のトルク、スラスト力及び電動機の電流の少なくとも一つを補助的に検出し、その結果と弁体の中間状態検出手段の検出結果を組み合わせることにより、より高精度な充填体形成の検出が可能となる。
(Function and effect)
As the material seal type feeder, a screw feeder using an electric motor as a drive source is suitable. In such a screw feeder, the friction resistance of the raw material supply and the torque of the screw shaft, the thrust force or the electric current of the electric motor have a correlation, and the formation of the raw material filler and the friction resistance of the raw material supply have a correlation. . That is, the torque of the screw shaft, the thrust force or the electric current of the electric motor and the formation of the raw material filler have a correlation. Therefore, when using the material seal type screw feeder, at least one of the torque of the screw shaft, the thrust force, and the electric current of the motor is supplementarily detected, and the result is combined with the detection result of the intermediate state detection means of the valve body. Therefore, it is possible to detect the formation of the filler with higher accuracy.

<請求項4記載の発明>
前記充填体がシール漏れしたか否かを検出するシール漏れ検出手段を備えており、
前記制御装置は、前記シール漏れ検出手段により前記充填体がシール漏れしたことが検出されたとき、前記背圧弁を閉じる制御を行うものである、請求項1記載の加圧容器供給装置。
<Invention of Claim 4>
A seal leak detecting means for detecting whether or not the filler has a seal leak;
2. The pressurized container supply device according to claim 1, wherein the control device performs control for closing the back pressure valve when it is detected by the seal leakage detection means that the filler has leaked. 3.

(作用効果)
充填体には上流側圧力と下流側圧力との差圧がかかっているため、原料の充填が不十分又は不均質である場合等に、充填体が崩壊等してシール漏れを起こすことがある。よって、上述のようにこのような事態を検出し、再度充填体の形成を促進するべく、背圧弁を閉じるのが好ましい。充填体が形成されると、前述の本発明の制御により自動的に背圧弁が開となり、円滑に定常運転に復帰させることができる。
(Function and effect)
Since the differential pressure between the upstream pressure and the downstream pressure is applied to the filling body, the filling body may collapse or cause seal leakage when the raw material is insufficiently filled or heterogeneous. . Therefore, it is preferable to close the back pressure valve in order to detect such a situation as described above and promote the formation of the filler again. When the filling body is formed, the back pressure valve is automatically opened by the above-described control of the present invention, and can be smoothly returned to the steady operation.

<請求項5記載の発明>
前記シール漏れ検出手段は、前記加圧容器の内圧を計測する内圧計であり、前記制御装置は、この内圧計による計測値が所定時間内に所定値以上減少したとき、前記背圧弁を閉じる制御を行うものである、請求項4記載の連続供給型反応装置。
<Invention of Claim 5>
The seal leak detection means is an internal pressure gauge that measures the internal pressure of the pressurized container, and the control device controls the closing of the back pressure valve when a measured value by the internal pressure gauge decreases by a predetermined value or more within a predetermined time. The continuous supply type reactor according to claim 4, wherein

(作用効果)
シール漏れ検出手段は適宜定めることができるが、原料の供給先が加圧容器であり、通常このような加圧容器には内圧計が設けられることが多く、シール漏れは内圧の急激な減少として現れるため、上述のように加圧容器の内圧が急激に減少したときに背圧弁を閉じる制御を行うことが望ましい。
(Function and effect)
The seal leak detection means can be determined as appropriate, but the supply destination of the raw material is a pressurized container, and such a pressurized container is usually provided with an internal pressure gauge, and the seal leak is a rapid decrease of the internal pressure. Therefore, as described above, it is desirable to perform control to close the back pressure valve when the internal pressure of the pressurized container is rapidly reduced.

<請求項6記載の発明>
前記加圧容器は、内部温度が前記充填体の上流側の温度より高いものであり、
前記シール漏れ検出手段は、前記供給管路における前記充填体の充填領域よりも上流側における排気温度を計測する上流側排気温度計であり、この上流側排気温度計による計測値が所定温度以上に上昇したとき、前記背圧弁を閉じる制御を行うものである、請求項4又は5記載の加圧容器供給装置。
<Invention of Claim 6>
The pressurized container has an internal temperature higher than the temperature upstream of the filler,
The seal leakage detection means is an upstream exhaust thermometer that measures an exhaust temperature upstream of a filling region of the filler in the supply pipe line, and a measured value by the upstream exhaust thermometer exceeds a predetermined temperature. The pressurization container supply device according to claim 4 or 5 which performs control which closes said back pressure valve when it raises.

(作用効果)
加圧容器が高温で反応を行う容器である場合等においては、加圧容器の内部温度が充填体の上流側の温度より高くなる場合がある。このような場合に充填体のシール漏れが発生すると、充填体の上流側の温度が上昇するため、上述のように充填体の上流側における排気口の温度が上昇したときに背圧弁の閉制御を行うのも好ましい形態である。
(Function and effect)
When the pressurized container is a container that reacts at a high temperature, the internal temperature of the pressurized container may be higher than the temperature on the upstream side of the filler. In such a case, if the seal leakage of the filling body occurs, the temperature on the upstream side of the filling body rises. Therefore, when the temperature of the exhaust port on the upstream side of the filling body rises as described above, the back pressure valve closing control is performed. It is also a preferable form to perform.

<請求項7記載の発明>
前記制御装置は、前記充填体のシール漏れ検出により前記背圧弁を閉じるとき、その後所定時間経過するまでは前記中間状態検出手段により前記中間状態にあることが検出されたときでも前記背圧弁を開けない制御を行うものである、請求項4〜6のいずれか1項に記載の加圧容器供給装置。
<Invention of Claim 7>
The control device opens the back pressure valve when the back pressure valve is closed by detecting the seal leak of the filler, even when the intermediate state detecting means detects that the intermediate state is detected until a predetermined time elapses thereafter. The pressurization container supply apparatus of any one of Claims 4-6 which performs what control is not performed.

(作用効果)
シール漏れ検出により背圧弁を閉じるときに一定以上の時間を要すると、その間に背圧弁の中間状態が検出されて背圧弁を開ける制御がなされるおそれがある。この場合、シール漏れが改善されないため、このシール漏れを再度検出することにより再び背圧弁を閉じる制御を行うことになり、その結果として背圧弁の開閉を繰り返すおそれがある。よって、上述のように、充填体のシール漏れ検出により背圧弁を閉じるときには、その後所定時間経過するまで、中間状態検出手段により中間状態にあることが検出されたときでも背圧弁を開けない制御を行うのが好ましい。これにより、背圧弁が開閉を繰り返すといった事態を防止できるようになる。
(Function and effect)
If a certain amount of time is required when closing the back pressure valve due to seal leak detection, an intermediate state of the back pressure valve may be detected during that time and control to open the back pressure valve may be performed. In this case, since the seal leak is not improved, the control for closing the back pressure valve again is performed by detecting the seal leak again, and as a result, the back pressure valve may be repeatedly opened and closed. Therefore, as described above, when the back pressure valve is closed by detecting the seal leak of the filler, control is performed so that the back pressure valve is not opened even when the intermediate state detecting means detects that the intermediate state is in the intermediate state until a predetermined time elapses thereafter. It is preferred to do so. As a result, a situation in which the back pressure valve repeatedly opens and closes can be prevented.

<請求項8記載の発明>
前記原料の固形分が木質バイオマスであり、前記加圧容器が木質バイオマスと希硫酸との加水分解反応を行う加圧反応容器であり、前記原料の液分が水である、請求項1〜7のいずれか1項に記載の加圧容器供給装置。
<Invention of Claim 8>
The solid content of the raw material is woody biomass, the pressure vessel is a pressure reaction vessel that performs a hydrolysis reaction between the woody biomass and dilute sulfuric acid, and the liquid content of the raw material is water. The pressurization container supply apparatus of any one of these.

(作用効果)
このような加圧容器内での木質バイオマス原料の加水分解では、原料固形分が粗く不均質であることが多いため、原供給開始当初の充填体の形成が比較的に困難であり、また充填体の上流側及び下流側の圧力差もある程度あるため、シール漏れを起こし易い。よって、本発明は、このような木質バイオマスを含む原料を希硫酸の存在下で加水分解する加圧反応容器に原料を供給する場合に好適である。
(Function and effect)
In the hydrolysis of woody biomass raw material in such a pressurized container, the raw material solids are often coarse and heterogeneous, so it is relatively difficult to form a packing at the beginning of raw supply, Since there is also a certain pressure difference between the upstream side and the downstream side of the body, seal leakage is likely to occur. Therefore, this invention is suitable when supplying a raw material to the pressurized reaction container which hydrolyzes the raw material containing such a woody biomass in presence of dilute sulfuric acid.

<請求項9記載の発明>
固液混合原料を、加圧容器内へ連続供給するとともに、この供給管路に前記原料の充填体を形成し、この充填体により供給管路の上流側圧力と下流側圧力とを遮断しつつ前記原料の供給を行う方法であって、
前記供給管路における前記充填体の充填領域の下流側に背圧弁を設け、
前記背圧弁の弁体が閉状態と開状態との間の中間状態にあるときに前記背圧弁を開ける、
ことを特徴とする加圧容器供給方法。
<Invention of Claim 9>
While the solid-liquid mixed raw material is continuously supplied into the pressurized container, a filling body of the raw material is formed in the supply pipe line, and the upstream side pressure and the downstream side pressure of the supply pipe line are blocked by the filling body. A method of supplying the raw material,
A back pressure valve is provided on the downstream side of the filling region of the filling body in the supply pipeline,
Opening the back pressure valve when the valve body of the back pressure valve is in an intermediate state between a closed state and an open state;
A pressurized container supply method characterized by the above.

(作用効果)
請求項1記載の発明と同様の作用効果が奏せられる。
(Function and effect)
The same effect as that of the first aspect of the invention can be achieved.

以上のとおり本発明によれば、充填体形成の誤検出、所要動力増、及び閉塞を防止できるようになる。   As described above, according to the present invention, it is possible to prevent erroneous detection of the filler formation, increase in required power, and blockage.

木質バイオマスエタノール設備例のフロー図である。It is a flowchart of the example of woody biomass ethanol equipment. 糖化反応装置の要部を示す概略図である。It is the schematic which shows the principal part of a saccharification reaction apparatus. 容器供給装置の要部拡大縦断面図である。It is a principal part expanded longitudinal cross-sectional view of a container supply apparatus. 制御装置のフローチャートである。It is a flowchart of a control apparatus. 容器供給装置の要部拡大縦断面図である。It is a principal part expanded longitudinal cross-sectional view of a container supply apparatus. 容器供給装置の要部拡大縦断面図である。It is a principal part expanded longitudinal cross-sectional view of a container supply apparatus. 容器供給装置の要部拡大縦断面図である。It is a principal part expanded longitudinal cross-sectional view of a container supply apparatus. 容器供給装置の要部拡大縦断面図である。It is a principal part expanded longitudinal cross-sectional view of a container supply apparatus.

以下、本発明の一実施形態について添付図面を参照しながら詳説する。
図1は、バガス、籾殻、稲藁、ウッドチップ(廃建材含む)等の木質系バイオマス(固形分)を洗浄機2により洗浄し、次いで脱水機3により水分率80〜85重量%程度まで脱水した後、加圧容器4において希硫酸触媒により加水分解し、グルコース、キシロース、アラビノース、ガラクトース、マンノース等のC5糖類を生成する糖化反応装置1と、この糖化反応装置1による生成物の液分を水平ベルトフィルター等のろ過装置11により回収し、中和槽12で消石灰を添加して中和した後に発酵槽13でエタノール発酵性大腸菌によりエタノール変換し、濃縮器14、蒸留塔15、脱水装置16を経てエタノールを回収するエタノール変換装置10とを有する木質バイオマスエタノール設備例を示している。この設備例では、ろ過装置11により回収される固形分である加水分解残渣(セルロース、リグニン)は例えばボイラー燃料として、あるいはコンポストとして利用される。
Hereinafter, an embodiment of the present invention will be described in detail with reference to the accompanying drawings.
FIG. 1 shows that woody biomass (solid content) such as bagasse, rice husk, rice straw, and wood chips (including waste building materials) is washed by the washing machine 2, and then dehydrated to a moisture content of about 80 to 85% by weight with the dehydrator 3. After that, the saccharification reaction apparatus 1 that generates C5 saccharides such as glucose, xylose, arabinose, galactose, and mannose by hydrolysis with a dilute sulfuric acid catalyst in the pressurized vessel 4 and the liquid fraction of the product by the saccharification reaction apparatus 1 It is collected by a filtration device 11 such as a horizontal belt filter, neutralized by adding slaked lime in a neutralization tank 12, and then ethanol-converted by an ethanol-fermenting Escherichia coli in a fermentation tank 13, a concentrator 14, a distillation tower 15, and a dehydrator 16. The example of the woody biomass ethanol installation which has the ethanol conversion apparatus 10 which collect | recovers ethanol via is shown. In this example of equipment, the hydrolysis residue (cellulose, lignin), which is a solid content recovered by the filtration device 11, is used as, for example, boiler fuel or compost.

糖化反応装置1の要部は図2に詳細に示されている。すなわち、脱水機3により脱水された固液混合原料は、先ずスクリューフィーダーからなる原料供給装置20により連続定量的に切り出されて、マテリアルシール型フィーダー及び背圧弁40を備えた容器供給装置30に供給され、この容器供給装置30より反応器としての加圧容器4に供給される。加圧容器4においては、その供給口4iから、容器供給装置30の排出管路31の上部に設けたノズル31nから噴射される蒸気及び希硫酸の混合物が原料とともに供給される。蒸気は反応温度を維持する役割を担う。この加圧容器4に対する希硫酸供給とともに又はこれに代えて、容器供給装置30よりも上流側において予め原料に希硫酸を混合し、原料固形分内への硫酸の浸透を促進することもできる。加圧容器4内には、スクリュータイプの撹拌搬送装置4wが供給口4i側から排出口4x側へ向かう方向に沿って架設されており、加圧容器4内に供給された原料はこの撹拌搬送装置4wにより撹拌搬送される過程において所定時間加圧容器4内に保持され、加水分解が進行し糖類が生成された後、反応物として排出される。   The main part of the saccharification reaction apparatus 1 is shown in detail in FIG. That is, the solid-liquid mixed raw material dehydrated by the dehydrator 3 is first continuously and quantitatively cut out by the raw material supply device 20 including a screw feeder and supplied to the container supply device 30 including the material seal type feeder and the back pressure valve 40. Then, this container supply device 30 supplies the pressurized container 4 as a reactor. In the pressurized container 4, a mixture of steam and dilute sulfuric acid sprayed from a nozzle 31n provided on the upper part of the discharge pipe 31 of the container supply apparatus 30 is supplied together with the raw material from the supply port 4i. Steam plays the role of maintaining the reaction temperature. Along with or in place of the dilute sulfuric acid supply to the pressurized container 4, dilute sulfuric acid may be mixed with the raw material in advance upstream of the container supply device 30 to promote permeation of sulfuric acid into the raw material solids. A screw type agitating / conveying device 4w is installed in the pressurized container 4 along the direction from the supply port 4i side to the discharge port 4x side, and the raw material supplied into the pressurized container 4 is agitated and conveyed. In the process of being stirred and transported by the apparatus 4w, it is held in the pressurized container 4 for a predetermined time, and after hydrolysis proceeds and saccharides are produced, they are discharged as reactants.

容器供給装置30の詳細は図3に示されている。この容器供給装置30は、加圧容4器の供給口4iに連通する縦方向に沿う排出管路31と、この排出管路31の側壁に連通する供給管路32を備えたマテリアルシール型フィーダーと、その供給管路32における先端部排出口32xを弁座としてこれを開閉する背圧弁40と、この背圧弁40の開閉駆動装置としてのシリンダー42とを備えるものである。   Details of the container supply device 30 are shown in FIG. This container supply device 30 includes a material seal type feeder provided with a discharge conduit 31 along the vertical direction communicating with the supply port 4i of the pressurized container 4 and a supply conduit 32 communicating with the side wall of the discharge conduit 31. A back pressure valve 40 that opens and closes the front end discharge port 32x in the supply pipe line 32 as a valve seat and a cylinder 42 as an opening and closing drive device for the back pressure valve 40 are provided.

より詳細には、図示例のマテリアルシール型フィーダーはいわゆるプラグスクリューフィーダーである。このフィーダーの供給管路32は横方向に沿って延在する形状をなし、基端側上部に供給口32i及び先端面に排出口32xをそれぞれ有し、また、供給口32iから排出口に32x向かうにつれて内径が縮小する縮径領域32yと、この縮径領域32yの先端側に隣接する縮径領域32y以下の内径を有する充填領域32zとを有している。縮径領域32yは二重管状をなしており、内管32iの周壁には略その全体にわたり多数の図示しない貫通口が形成されるとともに、外管32cの上部に排気口32e及び下部に排液口32dがそれぞれ設けられている。供給管路32内には、スクリュー軸33が同心状に軸装されており、電動機からなる回転駆動源34により回転駆動されるように構成されている。もちろん、本発明のマテリアルシール型フィーダーは、この例に限定されるものではなく、例えば、図示しないが、上述のスクリューによる原料押し込みに代えてピストンによる原料押し込みを採用したマテリアルシール型ピストンフィーダーを用いることもできる。   More specifically, the illustrated material seal type feeder is a so-called plug screw feeder. The feeder supply pipe 32 has a shape extending in the lateral direction, and has a supply port 32i at the upper part on the base end side and a discharge port 32x at the distal end surface, and 32x from the supply port 32i to the discharge port. It has a reduced diameter area 32y whose inner diameter is reduced as it goes, and a filling area 32z having an inner diameter equal to or smaller than the reduced diameter area 32y adjacent to the distal end side of the reduced diameter area 32y. The reduced diameter region 32y has a double tubular shape, and a large number of through-holes (not shown) are formed in the peripheral wall of the inner tube 32i almost entirely, and an exhaust port 32e is discharged above the outer tube 32c and drained at the lower portion. Each port 32d is provided. A screw shaft 33 is concentrically mounted in the supply pipe line 32 and is configured to be rotationally driven by a rotational drive source 34 formed of an electric motor. Of course, the material seal type feeder of the present invention is not limited to this example. For example, although not shown, a material seal type piston feeder that employs material pushing by a piston instead of pushing the material pushing by the screw described above is used. You can also.

背圧弁40は供給管路32の先端排出口32xを開閉する円錐状の弁体41と、この弁体41を供給管路32の先端排出口32xに対して対向方向に進退させるシリンダー42とを備えているものである。弁体41は後方に突出する支持軸43を有しており、この支持軸43が排出管路31の側壁を貫通して排出管路31外部に突出し、排出管路31の外面に取り付けられたシリンダー42の伸縮軸に対して直列的に連結されている。したがって、弁体41が閉位置にあるときには弁体41はシリンダー42の内圧により閉方向に付勢される。   The back pressure valve 40 includes a conical valve body 41 that opens and closes the tip discharge port 32x of the supply pipe line 32, and a cylinder 42 that advances and retracts the valve body 41 in a direction opposite to the tip discharge port 32x of the supply pipe line 32. It is what it has. The valve body 41 has a support shaft 43 that protrudes rearward. The support shaft 43 penetrates the side wall of the discharge pipe 31 and protrudes to the outside of the discharge pipe 31, and is attached to the outer surface of the discharge pipe 31. The cylinder 42 is connected in series to the telescopic shaft. Therefore, when the valve body 41 is in the closed position, the valve body 41 is urged in the closing direction by the internal pressure of the cylinder 42.

特徴的には、弁体支持軸43における排出管路31の外部に突出する部分にカラーが取り付けられて当接部44が形成されており、弁体41が閉状態にあるときにこの当接部44が接触してオンとなり、且つ弁体41が閉状態と開状態との間の中間状態にあるときにこの当接部44が接触せずにオフとなる位置に閉リミットスイッチ50を取り付けている。また、本例では、弁体41が開状態にあるときにこの当接部44が接触してオンとなり、且つ弁体41が閉状態と開状態との間の中間状態にあるときにこの当接部44が接触せずにオフとなる位置に開リミットスイッチ51も取り付けている。なお、弁体41の位置を検出できるものであれば、本例のリミットスイッチ50,51に代えて非接触タイプのセンサ等、他の公知の検出器を用いることも可能である。   Characteristically, a collar is attached to a portion of the valve body support shaft 43 that protrudes outside the discharge pipe 31 to form a contact portion 44, and this contact is made when the valve body 41 is in a closed state. The closed limit switch 50 is mounted at a position where the contact portion 44 is turned on without being in contact with the contact portion 44 when the contact portion 44 is turned on and the valve body 41 is in an intermediate state between the closed state and the open state. ing. Further, in this example, when the valve body 41 is in the open state, the contact portion 44 comes into contact and is turned on, and when the valve body 41 is in an intermediate state between the closed state and the open state, An open limit switch 51 is also attached at a position where the contact portion 44 is turned off without contact. As long as the position of the valve body 41 can be detected, other known detectors such as a non-contact type sensor can be used instead of the limit switches 50 and 51 of this example.

また、特徴的には、容器供給装置30は、図4に示すフローチャートにしたがって背圧弁開閉制御を行う制御装置(図示略)を備えている。すなわち、この容器供給装置30において原料供給を開始する際には、先ずシリンダー42により背圧弁40を閉じた後、スクリュー軸33を始動させて固液混合原料Mを先端側に移送する。図5に示すように、供給管路32の排出口32xは背圧弁40により閉じられており、圧力だけでなく原料Mの移動も弁体41により遮断されているため、次第に供給管路32内に固液混合原料Mが充満し、後続原料Mによる押し込み力と、縮径領域32yにおける内径減少とによって、供給管路32の先端側から順に原料Mが強く圧縮されるようになる。この圧縮がある程度まで進行すると、図6に示すように充填領域32zに原料が気密充填されて充填体Pが形成された後、図7に示すようにこの充填体Pが背圧弁40の弁体41の押し付け力に抗して弁体41を押し開く。このとき、弁体支持軸43の当接部44が閉リミットスイッチ50から離間することにより閉リミットスイッチ50がオフとなり弁体41が中間状態にあることが検出される。制御装置は中間状態が検出されると、充填体Pが形成されたものと判断して図8に示すように背圧弁40を開ける制御を行う。この中間状態の検出は、原料供給Mの摩擦抵抗に関係なく、しかも充填体Pの形成と直接に関係するため、充填体Pの形成が的確に検出される。よって、充填体形成の誤検出、所要動力増、及び閉塞を防止できるようになる。   Characteristically, the container supply device 30 includes a control device (not shown) that performs back pressure valve opening / closing control according to the flowchart shown in FIG. That is, when starting the supply of raw materials in the container supply device 30, first, the back pressure valve 40 is closed by the cylinder 42, and then the screw shaft 33 is started to transfer the solid-liquid mixed raw material M to the front end side. As shown in FIG. 5, the discharge port 32x of the supply line 32 is closed by a back pressure valve 40, and not only the pressure but also the movement of the raw material M is blocked by the valve body 41. The solid-liquid mixed raw material M is filled, and the raw material M is strongly compressed in order from the front end side of the supply pipe line 32 by the pushing force by the subsequent raw material M and the inner diameter reduction in the reduced diameter region 32y. When this compression proceeds to a certain extent, after the raw material is hermetically filled in the filling region 32z as shown in FIG. 6 to form the filling body P, the filling body P is used as the valve body of the back pressure valve 40 as shown in FIG. The valve element 41 is pushed open against the pressing force of 41. At this time, when the contact portion 44 of the valve body support shaft 43 is separated from the closed limit switch 50, it is detected that the closed limit switch 50 is turned off and the valve body 41 is in an intermediate state. When the intermediate state is detected, the control device determines that the filler P has been formed, and performs control to open the back pressure valve 40 as shown in FIG. Since the detection of this intermediate state is directly related to the formation of the filler P regardless of the frictional resistance of the raw material supply M, the formation of the filler P is accurately detected. Therefore, it is possible to prevent erroneous detection of the filling body formation, increase in required power, and blockage.

このようにして、供給管路32の排出口32xからは順次原料充填体Pの下流側部分が排出され、排出管路31を介して加圧容器4に投入される定常運転状態となる。定常運転状態では、図8に示すように充填体Pは下流側から順に排出されるが、上流側では新たに押し込まれる原料により成長するため、その長さ及びシール性能は維持される。   In this way, the downstream portion of the raw material filler P is sequentially discharged from the discharge port 32x of the supply pipe 32, and a steady operation state in which the pressurized container 4 is charged through the discharge pipe 31 is achieved. In the steady operation state, as shown in FIG. 8, the filler P is discharged in order from the downstream side, but on the upstream side, it grows with the newly pushed raw material, so its length and sealing performance are maintained.

他方、このような定常運転状態にあるとき、充填体Pには上流側圧力と下流側圧力との差圧がかかっているため、原料の充填が不十分又は不均質である場合等に、充填体Pが崩壊等してシール漏れを起こすことがある。よって、充填体Pがシール漏れしたか否かを検出するシール漏れ検出手段を設け、図4に示すように、このような事態が検出されたときには制御装置が背圧弁40を閉じて、再度充填体の形成を促進するのが好ましい。このシール漏れ検出手段は適宜定めることができるが、原料の供給先が加圧容器4であり、通常このような加圧容器4には内圧計4p(図2参照)が設けられることが多く、シール漏れは内圧の急激な減少として現れるため、加圧容器4の内圧が急激に減少したとき、つまり内圧計4pによる計測値が所定時間内に所定値以上減少したときに背圧弁40を閉じる制御を行うことが望ましい。   On the other hand, when in such a steady operation state, since the differential pressure between the upstream pressure and the downstream pressure is applied to the filling body P, the filling is performed when the raw material is insufficiently filled or heterogeneous. The body P may collapse and cause seal leakage. Therefore, a seal leak detecting means for detecting whether or not the filler P has leaked is provided. As shown in FIG. 4, when such a situation is detected, the controller closes the back pressure valve 40 and refills. It is preferred to promote body formation. Although this seal leak detection means can be determined as appropriate, the supply destination of the raw material is the pressurized container 4, and such a pressurized container 4 is usually provided with an internal pressure gauge 4p (see FIG. 2). Since the seal leakage appears as a rapid decrease in internal pressure, the back pressure valve 40 is controlled to close when the internal pressure of the pressurized container 4 decreases rapidly, that is, when the measured value by the internal pressure gauge 4p decreases by a predetermined value or more within a predetermined time. It is desirable to do.

また、本例のように加圧容器4が高温で反応を行う容器である場合、加圧容器4の内部温度が充填体Pの上流側の温度より高く、このような場合に充填体Pのシール漏れが発生すると、充填体Pの上流側の温度が上昇する。よって、シール漏れ検出手段として、充填領域32zよりも上流側における排気温度を計測する上流側排気温度計30tを設け、この計測温度が上昇したときに背圧弁40の閉制御を行うのも好ましい形態である。   Moreover, when the pressurized container 4 is a container which reacts at high temperature like this example, the internal temperature of the pressurized container 4 is higher than the temperature of the upstream of the filler P, and in such a case, the filler P When seal leakage occurs, the temperature on the upstream side of the filler P increases. Therefore, it is also preferable to provide an upstream side exhaust thermometer 30t that measures the exhaust temperature upstream of the filling region 32z as the seal leak detection means, and to perform the closing control of the back pressure valve 40 when the measured temperature rises. It is.

このような制御により充填体Pが形成されると、前述の充填体形成時の制御により自動的に背圧弁40が開となり、円滑に定常運転に復帰させることができる。ただし、シール漏れ検出により背圧弁40を閉じるときに一定以上の時間を要すると、この間に背圧弁40の中間状態が検出されると背圧弁40を開ける制御と、シール漏れによる背圧弁40の閉制御とが繰り返されるおそれがある。よって、図4に示すように、充填体Pのシール漏れ検出により背圧弁40を閉じるときには、その後遅延タイマーを作動させ、所定時間経過するまでは、中間状態検出手段により中間状態にあることが検出されたときでも背圧弁40を開けない制御を行うのは好ましい。これにより、背圧弁40が開閉を繰り返すといった事態を防止できるようになる。   When the filling body P is formed by such control, the back pressure valve 40 is automatically opened by the above-described control at the time of forming the filling body, and can be smoothly returned to the steady operation. However, if it takes a certain amount of time to close the back pressure valve 40 due to the detection of the seal leak, the control to open the back pressure valve 40 when the intermediate state of the back pressure valve 40 is detected during this time, and the closing of the back pressure valve 40 due to the seal leak. Control may be repeated. Therefore, as shown in FIG. 4, when the back pressure valve 40 is closed by detecting the seal leak of the filler P, the delay timer is operated thereafter, and the intermediate state detecting means detects that the intermediate state is in the intermediate state until a predetermined time elapses. It is preferable to perform control so that the back pressure valve 40 is not opened even when it is performed. Thereby, the situation where the back pressure valve 40 repeats opening and closing can be prevented.

<その他>
上記例のようなスクリューフィーダーでは、原料供給の摩擦抵抗と、スクリュー軸33のトルク、スラスト力または電動機34の電流とは相関関係を有し、原料充填体Pの形成と原料供給の摩擦抵抗とは相関関係を有する。つまり、スクリュー軸33のトルク、スラスト力または電動機34の電流と原料充填体Pの形成とは相関関係を有する。したがって、上記例のように、プラグスクリューフィーダーを用いる場合、スクリュー軸33のトルクを検出するトルク検出器(図示略)、スクリュー軸33のスラスト力を検出するスラスト力検出器(図示略)及び電動機34の電流を検出する電流検出器34mのうち少なくとも一つの補助検出手段を設け、この補助検出手段の測定結果と弁体41の中間状態検出手段の検出結果を組み合わせて、補助検出手段による検出値が所定値以上であって、なおかつ中間状態検出手段により背圧弁40の弁体41が中間状態にあることが検出されたときにシリンダー42により背圧弁40を開ける制御を行うことにより、より高精度な充填体形成の検出が可能となる。
<Others>
In the screw feeder as in the above example, the friction resistance of the raw material supply and the torque of the screw shaft 33, the thrust force, or the current of the electric motor 34 have a correlation, and the formation of the raw material filler P and the friction resistance of the raw material supply Have a correlation. That is, the torque of the screw shaft 33, the thrust force, or the current of the electric motor 34 and the formation of the raw material filler P have a correlation. Therefore, when using a plug screw feeder as in the above example, a torque detector (not shown) for detecting the torque of the screw shaft 33, a thrust force detector (not shown) for detecting the thrust force of the screw shaft 33, and an electric motor 34. At least one auxiliary detection means is provided in the current detector 34m for detecting the current 34, and the detection value by the auxiliary detection means is obtained by combining the measurement result of the auxiliary detection means and the detection result of the intermediate state detection means of the valve body 41. Is more accurate by controlling the cylinder 42 to open the back pressure valve 40 when the intermediate state detecting means detects that the valve body 41 of the back pressure valve 40 is in the intermediate state. It is possible to detect the formation of a filler.

本発明は、木質系バイオマスの糖化における加圧反応容器への原料供給に好適であるが、これに限られず他の加圧容器への原料供給の用途にも適用できることはいうまでもない。   Although this invention is suitable for the raw material supply to the pressurization reaction container in saccharification of woody biomass, it cannot be overemphasized that it can apply also to the use of the raw material supply to another pressurization container.

1…糖化反応装置、2…洗浄機、3…脱水機、4…加圧容器、10…エタノール変換装置、20…原料供給装置、30…加圧容器供給装置、40…背圧弁。   DESCRIPTION OF SYMBOLS 1 ... Saccharification reaction apparatus, 2 ... Washing machine, 3 ... Dehydrator, 4 ... Pressurization container, 10 ... Ethanol conversion apparatus, 20 ... Raw material supply apparatus, 30 ... Pressurization container supply apparatus, 40 ... Back pressure valve.

以下、本発明の一実施形態について添付図面を参照しながら詳説する。
図1は、バガス、籾殻、稲藁、ウッドチップ(廃建材含む)等の木質系バイオマス(固形分)を洗浄機2により洗浄し、次いで脱水機3により水分率80〜85重量%程度まで脱水した後、加圧容器4において希硫酸触媒により加水分解し、グルコース、ガラクトース、マンノース等のC6糖類や、キシロース、アラビノース等のC5糖類を生成する糖化反応装置1と、この糖化反応装置1による生成物の液分を水平ベルトフィルター等のろ過装置11により回収し、中和槽12で消石灰を添加して中和した後に発酵槽13でエタノール発酵性大腸菌によりエタノール変換し、濃縮器14、蒸留塔15、脱水装置16を経てエタノールを回収するエタノール変換装置10とを有する木質バイオマスエタノール設備例を示している。この設備例では、ろ過装置11により回収される固形分である加水分解残渣(セルロース、リグニン)は例えばボイラー燃料として、あるいはコンポストとして利用される。
Hereinafter, an embodiment of the present invention will be described in detail with reference to the accompanying drawings.
FIG. 1 shows that woody biomass (solid content) such as bagasse, rice husk, rice straw, and wood chips (including waste building materials) is washed by the washing machine 2, and then dehydrated to a moisture content of about 80 to 85% by weight with the dehydrator 3. After that, the saccharification reaction apparatus 1 generates C6 saccharides such as glucose, galactose and mannose, and C5 saccharides such as xylose and arabinose by hydrolysis with a dilute sulfuric acid catalyst in the pressurized container 4 and the production by the saccharification reaction apparatus 1 The liquid content of the product is collected by a filtration device 11 such as a horizontal belt filter, neutralized by adding slaked lime in a neutralization tank 12, and then ethanol-converted by an ethanol-fermenting Escherichia coli in a fermentation tank 13, a concentrator 14, and a distillation tower 15 shows an example of woody biomass ethanol equipment having an ethanol conversion device 10 that recovers ethanol through a dehydrating device 16. In this example of equipment, the hydrolysis residue (cellulose, lignin), which is a solid content recovered by the filtration device 11, is used as, for example, boiler fuel or compost.

Claims (9)

液分及び固形分からなる固液混合原料を、供給管路を介して加圧容器内へ連続供給するとともに、この供給管路に前記原料を気密充填してなる充填体を形成し、この充填体により供給管路の上流側圧力と下流側圧力とを遮断しつつ前記原料の供給を行う、マテリアルシール型のフィーダーと、
このフィーダーの供給管路における前記充填体の充填領域の下流側に設けられた背圧弁と、
この背圧弁の開閉駆動装置と、
を備えた加圧容器供給装置であって、
前記背圧弁の弁体が閉状態と開状態との間の中間状態にあるか否かを検出する中間状態検出手段と、
この中間状態検出手段により前記背圧弁の弁体が前記中間状態にあることが検出されたときに前記開閉駆動装置により前記背圧弁を開ける制御を行う制御装置と、
を備えたことを特徴とする加圧容器供給装置。
A solid-liquid mixed raw material composed of a liquid and a solid is continuously supplied into a pressurized container through a supply pipe, and a filling body is formed by hermetically filling the raw material in the supply pipe. A material seal type feeder that supplies the raw material while blocking the upstream pressure and the downstream pressure of the supply pipe by
A back pressure valve provided on the downstream side of the filling region of the filler in the feeder supply line;
An opening / closing drive for the back pressure valve;
A pressurized container supply device comprising:
Intermediate state detection means for detecting whether or not the valve body of the back pressure valve is in an intermediate state between a closed state and an open state;
A control device for performing control to open the back pressure valve by the opening / closing drive device when it is detected by the intermediate state detection means that the valve body of the back pressure valve is in the intermediate state;
A pressurized container supply device comprising:
前記中間状態検出手段は、前記背圧弁の弁体の移動力により、前記背圧弁の弁体が前記閉状態にあるときと前記中間状態にあるときとでオン/オフが切り替わる閉リミットスイッチである、請求項1記載の加圧容器供給装置。   The intermediate state detection means is a closed limit switch that is turned on / off depending on the moving force of the valve body of the back pressure valve when the valve body of the back pressure valve is in the closed state and when in the intermediate state. The pressurized container supply device according to claim 1. 前記フィーダーは、前記充填体の充填領域に向かって次第に内径が減少するように構成された前記供給管路と、この供給管路内に管軸方向に沿って設置されたスクリューと、このスクリューを回転駆動する電動機とを備えたプラグスクリューフィーダーであり、
前記中間状態検出手段に加えて、次の(イ)〜(ハ)の少なくとも一つの補助検出手段を備えており、
(イ)前記スクリュー軸のトルクを検出するトルク検出器、
(ロ)前記スクリュー軸のスラスト力を検出するスラスト力検出器、
(ハ)前記電動機の電流を検出する電流検出器、
前記制御装置は、補助検出手段による検出値が所定値以上であって、なおかつ前記中間状態検出手段により前記背圧弁の弁体が前記中間状態にあることが検出されたときに前記開閉駆動装置により前記背圧弁を開ける制御を行うものである、
請求項1又は2記載の加圧容器供給装置。
The feeder includes the supply pipe configured so that the inner diameter gradually decreases toward the filling region of the filler, a screw installed in the supply pipe along the pipe axis direction, and the screw. A plug screw feeder equipped with an electric motor for rotational driving,
In addition to the intermediate state detection means, it comprises at least one auxiliary detection means of the following (A) to (C):
(A) a torque detector for detecting the torque of the screw shaft;
(B) a thrust force detector for detecting a thrust force of the screw shaft;
(C) a current detector for detecting the current of the motor;
When the detected value by the auxiliary detecting means is equal to or greater than a predetermined value and the intermediate state detecting means detects that the valve body of the back pressure valve is in the intermediate state, the control device uses the opening / closing drive device. Control to open the back pressure valve,
The pressurized container supply apparatus according to claim 1 or 2.
前記充填体がシール漏れしたか否かを検出するシール漏れ検出手段を備えており、
前記制御装置は、前記シール漏れ検出手段により前記充填体がシール漏れしたことが検出されたとき、前記背圧弁を閉じる制御を行うものである、請求項1記載の加圧容器供給装置。
A seal leak detecting means for detecting whether or not the filler has a seal leak;
2. The pressurized container supply device according to claim 1, wherein the control device performs control for closing the back pressure valve when it is detected by the seal leakage detection means that the filler has leaked. 3.
前記シール漏れ検出手段は、前記加圧容器の内圧を計測する内圧計であり、前記制御装置は、この内圧計による計測値が所定時間内に所定値以上減少したとき、前記背圧弁を閉じる制御を行うものである、請求項4記載の連続供給型反応装置。   The seal leak detection means is an internal pressure gauge that measures the internal pressure of the pressurized container, and the control device controls the closing of the back pressure valve when a measured value by the internal pressure gauge decreases by a predetermined value or more within a predetermined time. The continuous supply type reactor according to claim 4, wherein 前記加圧容器は、内部温度が前記充填体の上流側の温度より高いものであり、
前記シール漏れ検出手段は、前記供給管路における前記充填体の充填領域よりも上流側に設けられた排気口の排気温度を計測する上流側排気温度計であり、この上流側排気温度計による計測値が所定温度以上に上昇したとき、前記背圧弁を閉じる制御を行うものである、請求項4又は5記載の加圧容器供給装置。
The pressurized container has an internal temperature higher than the temperature upstream of the filler,
The seal leak detection means is an upstream exhaust thermometer that measures an exhaust temperature of an exhaust port provided upstream of a filling region of the filler in the supply pipeline, and is measured by the upstream exhaust thermometer. The pressurization container supply device according to claim 4 or 5 which performs control which closes said back pressure valve when a value rises above a predetermined temperature.
前記制御装置は、前記充填体のシール漏れ検出により前記背圧弁を閉じたとき、その後所定時間経過するまでは前記中間状態検出手段により前記中間状態にあることが検出されたときでも前記背圧弁を閉じない制御を行うものである、請求項4〜6のいずれか1項に記載の加圧容器供給装置。   The controller closes the back pressure valve when the back pressure valve is closed by detecting a seal leak of the filling body, and when the intermediate state detecting means detects that the back state is in the intermediate state until a predetermined time thereafter. The pressurized container supply apparatus of any one of Claims 4-6 which performs control which does not close. 前記原料の固形分が木質バイオマスであり、前記加圧容器が木質バイオマスと希硫酸との加水分解反応を行う加圧反応容器であり、前記原料の液分が水である、請求項1〜7のいずれか1項に記載の加圧容器供給装置。   The solid content of the raw material is woody biomass, the pressure vessel is a pressure reaction vessel that performs a hydrolysis reaction between the woody biomass and dilute sulfuric acid, and the liquid content of the raw material is water. The pressurization container supply apparatus of any one of these. 固液混合原料を、加圧容器内へ連続供給するとともに、この供給管路に前記原料の充填体を形成し、この充填体により供給管路の上流側圧力と下流側圧力とを遮断しつつ前記原料の供給を行う方法であって、
前記供給管路における前記充填体の充填領域の下流側に背圧弁を設け、
前記背圧弁の弁体が閉状態と開状態との間の中間状態にあるときに前記背圧弁を開ける、
ことを特徴とする加圧容器供給方法。
While the solid-liquid mixed raw material is continuously supplied into the pressurized container, a filling body of the raw material is formed in the supply pipe line, and the upstream side pressure and the downstream side pressure of the supply pipe line are blocked by the filling body. A method of supplying the raw material,
A back pressure valve is provided on the downstream side of the filling region of the filling body in the supply pipeline,
Opening the back pressure valve when the valve body of the back pressure valve is in an intermediate state between a closed state and an open state;
A pressurized container supply method characterized by the above.
JP2010120299A 2010-05-26 2010-05-26 Pressurized container supply apparatus and method Active JP5425706B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2010120299A JP5425706B2 (en) 2010-05-26 2010-05-26 Pressurized container supply apparatus and method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2010120299A JP5425706B2 (en) 2010-05-26 2010-05-26 Pressurized container supply apparatus and method

Publications (2)

Publication Number Publication Date
JP2011245410A true JP2011245410A (en) 2011-12-08
JP5425706B2 JP5425706B2 (en) 2014-02-26

Family

ID=45411329

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2010120299A Active JP5425706B2 (en) 2010-05-26 2010-05-26 Pressurized container supply apparatus and method

Country Status (1)

Country Link
JP (1) JP5425706B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102962008A (en) * 2012-11-29 2013-03-13 宜兴市昌吉利化工有限公司 Device for continuously producing alkyl-lithium lithium feeder
KR101431699B1 (en) 2013-01-24 2014-08-26 영남대학교 산학협력단 Solid particle feeding apparatus and its feeding method
WO2014132410A1 (en) * 2013-02-28 2014-09-04 三菱重工メカトロシステムズ株式会社 Raw-material supply device and biomass separation device
SE1850144A1 (en) * 2018-02-09 2019-08-10 Valmet Oy A system for transporting biomass material and a method for preventing blow back in said system
WO2020009634A1 (en) * 2018-07-02 2020-01-09 Valmet Ab Feeding system and method for feeding comminuted cellulosic material to a high-pressure treatment zone
CN115846229A (en) * 2022-11-18 2023-03-28 徐州铸烁工程检测技术有限公司 Intelligent electromechanical automatic feeding structure

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5211788U (en) * 1975-07-12 1977-01-27
JPS6081385A (en) * 1983-10-05 1985-05-09 宝酒造株式会社 High pressure continuous supply method and apparatus of material
JPH09183516A (en) * 1995-12-29 1997-07-15 Kurosaki Refract Co Ltd Screw-conveying machine and its control method
WO2004105927A2 (en) * 2003-06-02 2004-12-09 Jgc Corp High-pressure treatment apparatus and method of operating high-pressure treatment apparatus
JP2006281037A (en) * 2005-03-31 2006-10-19 Tsukishima Kikai Co Ltd Continuously-feedable reaction apparatus and method thereof
JP2007050357A (en) * 2005-08-18 2007-03-01 Toshiba Corp Waste treatment system
JP2007528479A (en) * 2003-04-30 2007-10-11 株式会社荏原製作所 Combustible raw material supply device, combustible raw material gasifier, and combustible raw material gasification method

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5211788U (en) * 1975-07-12 1977-01-27
JPS6081385A (en) * 1983-10-05 1985-05-09 宝酒造株式会社 High pressure continuous supply method and apparatus of material
JPH09183516A (en) * 1995-12-29 1997-07-15 Kurosaki Refract Co Ltd Screw-conveying machine and its control method
JP2007528479A (en) * 2003-04-30 2007-10-11 株式会社荏原製作所 Combustible raw material supply device, combustible raw material gasifier, and combustible raw material gasification method
WO2004105927A2 (en) * 2003-06-02 2004-12-09 Jgc Corp High-pressure treatment apparatus and method of operating high-pressure treatment apparatus
JP2006281037A (en) * 2005-03-31 2006-10-19 Tsukishima Kikai Co Ltd Continuously-feedable reaction apparatus and method thereof
JP2007050357A (en) * 2005-08-18 2007-03-01 Toshiba Corp Waste treatment system

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102962008A (en) * 2012-11-29 2013-03-13 宜兴市昌吉利化工有限公司 Device for continuously producing alkyl-lithium lithium feeder
KR101431699B1 (en) 2013-01-24 2014-08-26 영남대학교 산학협력단 Solid particle feeding apparatus and its feeding method
WO2014132410A1 (en) * 2013-02-28 2014-09-04 三菱重工メカトロシステムズ株式会社 Raw-material supply device and biomass separation device
AU2013380114B2 (en) * 2013-02-28 2016-06-23 Mitsubishi Power Environmental Solutions, Ltd. Raw-material supply device and biomass separation device
JP6053913B2 (en) * 2013-02-28 2016-12-27 三菱日立パワーシステムズ環境ソリューション株式会社 Raw material supply device and biomass decomposition device
US9994996B2 (en) 2013-02-28 2018-06-12 Mitsubishi Hitachi Power Systems Environmental Solutions, Ltd. Raw-material supply device and biomass separation device
SE1850144A1 (en) * 2018-02-09 2019-08-10 Valmet Oy A system for transporting biomass material and a method for preventing blow back in said system
WO2019156605A1 (en) 2018-02-09 2019-08-15 Valmet Ab A system for transporting biomass material and a method for preventing blow back in said system
WO2020009634A1 (en) * 2018-07-02 2020-01-09 Valmet Ab Feeding system and method for feeding comminuted cellulosic material to a high-pressure treatment zone
EP3817996A4 (en) * 2018-07-02 2022-04-06 Valmet Ab Feeding system and method for feeding comminuted cellulosic material to a high-pressure treatment zone
CN115846229A (en) * 2022-11-18 2023-03-28 徐州铸烁工程检测技术有限公司 Intelligent electromechanical automatic feeding structure
CN115846229B (en) * 2022-11-18 2023-10-20 徐州铸烁工程检测技术有限公司 Intelligent electromechanical automatic feeding structure

Also Published As

Publication number Publication date
JP5425706B2 (en) 2014-02-26

Similar Documents

Publication Publication Date Title
JP5425706B2 (en) Pressurized container supply apparatus and method
US20110308141A1 (en) Methods and devices for continuous transfer of particulate and/or fibrous material between two zones with different temperatures and pressures
NO338634B1 (en) Sludge treatment device and method
US20160215448A1 (en) Improved device for discharging pretreated biomass from higher to lower pressure regions
CN116272819B (en) Esterification reaction kettle for photoresist production
JP4873602B2 (en) Continuous feed reactor and method thereof
CN213022483U (en) A sampling equipment for fermented glutinous rice fermentation degree detects
CN101639373B (en) Method and device for measuring circulating flow rate of material of circulating fluidized bed
US20120040328A1 (en) Fermenter feed system for fermentable biomass of a biogas system and method for operating the feed system
US4273035A (en) Method and apparatus for stabilizing operation of a press
CN203043640U (en) Water-borne wood paint defoaming equipment capable of controlling automatically
CN209866061U (en) Continuous neutralization and layering system for mixed feed liquid after chlorination hydrolysis
CN211205914U (en) Continuous online quantitative sampling device of high-temperature high-pressure reaction kettle
CN202793831U (en) Automatic sampling device in chemical synthetic process
CN212639224U (en) Through discharging device parallel connection&#39;s buffer memory storehouse
CN106739087A (en) For the screw extruder of gas-explosive material dehydration
CN208267850U (en) A kind of extrusion system for push-bench correction
CN108445944B (en) Diene ring-opening reaction automatic control device
CN209649544U (en) Grid slag cleans squeezer
CN205011063U (en) Dry powder is thrown and is added machine
CN218307546U (en) A agitating unit for preparing low-cost ultrasonic inspection water base couplant
CN201283591Y (en) Extruding machine with full-automatic cooling apparatus
CN204996408U (en) Material proportion adjustment controlling means is thrown to reactor
CN204522372U (en) For the steam distillation tank that nicotine extracts
CN212530832U (en) Buffer storage bin with discharging device

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20121010

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20121109

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20121128

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20130823

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20130904

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20130927

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20131024

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: 20131115

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20131127

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

Ref document number: 5425706

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350