JPS61177928A - Culture of mushroom - Google Patents

Culture of mushroom

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Publication number
JPS61177928A
JPS61177928A JP60017607A JP1760785A JPS61177928A JP S61177928 A JPS61177928 A JP S61177928A JP 60017607 A JP60017607 A JP 60017607A JP 1760785 A JP1760785 A JP 1760785A JP S61177928 A JPS61177928 A JP S61177928A
Authority
JP
Japan
Prior art keywords
container
steam
bottle
sterilization
air
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
JP60017607A
Other languages
Japanese (ja)
Other versions
JPH0217129B2 (en
Inventor
萩原 四朗
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.)
GUNMA NETSU KANRI CENTER KK
Original Assignee
GUNMA NETSU KANRI CENTER KK
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 GUNMA NETSU KANRI CENTER KK filed Critical GUNMA NETSU KANRI CENTER KK
Priority to JP60017607A priority Critical patent/JPS61177928A/en
Publication of JPS61177928A publication Critical patent/JPS61177928A/en
Publication of JPH0217129B2 publication Critical patent/JPH0217129B2/ja
Granted legal-status Critical Current

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  • Mushroom Cultivation (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はビン等の容器中にて栽培する栽培きのこの製造
方法に関し、特に殺菌時間の短縮化、省エネルギー化に
特徴を有するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for producing cultivated mushrooms grown in containers such as bottles, and is particularly characterized by shortening sterilization time and saving energy.

(従来の技術) 従来はオガ屑に一定の水分を含有させ、その中に米ぬか
を相当量混入し、これをビン等の容器中に投入した後、
開放型の蒸気室又は圧力容器の中に入れて100℃から
120℃位で2時間から4時間殺菌した後に殖菌し芽出
し栽培を行っていた。
(Prior art) Conventionally, sawdust was made to contain a certain amount of moisture, a considerable amount of rice bran was mixed into it, and after this was put into a container such as a bottle,
The seeds were placed in an open steam chamber or pressure vessel and sterilized at about 100°C to 120°C for 2 to 4 hours, and then the bacteria were propagated and cultivated.

(発明が解決しようとする問題点) 従来のビン殺菌では蒸気による湿熱殺菌方法を利用して
、100℃前後の開放型加熱器や120℃前後の圧力容
器に入れて殺菌していたが、殺菌容器ビン中には多量の
空気が存在するために、圧力容器内は120℃であって
もビン容器中には温度差を生ずる。一方圧力容器内は高
温の湿熱であってもビン容器内は乾熱である。従って殺
菌効果は極めて悪い。すなわち、従来は湿熱殺菌と考え
られていた殺菌方法は、ビンは冷却されたまま加温室へ
入れられ外部より加熱されていたためにビン中の空気は
膨張した分だけ排出されていたが、その後は、一定温度
のままで加熱空気となり外部に排出されないために実質
的には乾熱殺菌されていたわけである。
(Problems to be Solved by the Invention) Conventional bottle sterilization uses a moist heat sterilization method using steam and is sterilized by placing the bottle in an open heater at around 100°C or a pressure vessel at around 120°C. Since a large amount of air exists in the container bottle, a temperature difference occurs in the bottle container even if the temperature inside the pressure container is 120°C. On the other hand, even though the inside of the pressure vessel is hot and moist, the inside of the bottle container is dry heat. Therefore, the bactericidal effect is extremely poor. In other words, in the sterilization method that was conventionally thought to be moist heat sterilization, the bottles were placed in a heating chamber while still being cooled and heated from the outside, so the air in the bottles was exhausted by the amount of expansion. Since the heated air remains at a constant temperature and is not discharged to the outside, it is essentially dry heat sterilized.

本発明は湿熱殺菌とすることにより好適な殺菌効果の向
上を図り理想的なきのこ栽培を行うとともに、併せて省
エネルギー効果をも充分に発揮することのできるきのこ
栽培方法を提供することを目的とする。
The purpose of the present invention is to provide a mushroom cultivation method that uses moist heat sterilization to improve the sterilization effect and perform ideal mushroom cultivation, and at the same time, can sufficiently exhibit the energy-saving effect. .

(問題を解決するための手段) 以上の問題は、ビン等の容器によるきのこ栽培方法にお
いて、容器中にオガ屑及び米ぬか等の所要材料を収納し
た後、前記容器中には蒸気を挿入し所要温度まで上昇さ
せることにより完全脱気し、脱気後は容器の開口部を閉
じ保温庫に入れ、これを保護することにより容器内の湿
熱殺菌を継続せしめ、その後殖菌し芽出し栽培を行うこ
とを特徴とするきのこ栽培方法によって解決される。
(Means for solving the problem) The above problem is caused by the method of cultivating mushrooms using a container such as a bottle.After the required materials such as sawdust and rice bran are stored in the container, steam is inserted into the container and the required amount is By raising the temperature to complete deaeration, after deaeration, close the opening of the container and place it in a heat-retaining chamber to protect it to continue moist heat sterilization inside the container, and then germination and budding cultivation. The problem is solved by a mushroom cultivation method characterized by:

(本発明の実施例) 本発明の第1の実施例を第1図に基づいて説明する。(Example of the present invention) A first embodiment of the present invention will be described based on FIG.

脱気の方法のため熱管理は、ボイラより送られて来た蒸
気は飽和蒸気のため温水を含有しているのでセパレータ
ー1で除去しトラップにて排出をすみやかに行い、乾き
蒸気を作り減圧弁2にて出来るだけ減圧しく現在の技術
では0 、2 kg / aJ )蒸気分配器3の中に
送るが、このとき更に減圧するために温度調節器4とセ
ンサー5及び電動バルブ6を用いて微低圧の蒸気を作り
分配器7の中の圧力を0.05 kg/−すなわち10
2〜103℃に保持する。ビン8の中に送気するための
導管9を分配器7から取出し、分配器側近に電磁弁10
を取付け、送気時間はタイマー11により任意の時間、
蒸気量を挿入することができる装置とし、このとき温度
調節器4では蒸気量の変動に対応できないので、電動バ
ルブ6と並列に電磁弁12を取付は分配器7後の電磁弁
10と同時に作動させることにより分配器7の圧力低下
を防ぐ。又蒸気の使用が中断した場合には分配器及び導
管の放熱により圧力低下があるが、これは温度調節器4
が働き、温度を一定に保持する機能を果たす。分配器7
から出た導管9は電磁弁10を通過して送気されるが、
電磁弁10の停止中は、送気されないので以降の導管は
冷却され導管9中の蒸気は水滴となり次回送気されると
きに水滴を挿入することになるので電磁弁以降の導管は
蒸気室13を貫通させ、送気されないときも保温され冷
却されない様にする。
Since the steam sent from the boiler is saturated steam and contains hot water, it is removed in separator 1 and quickly discharged in a trap to produce dry steam and then the pressure reducing valve is used for heat management. At step 2, the pressure is reduced as much as possible (according to current technology, 0.2 kg/aJ) and sent into the steam distributor 3. At this time, in order to further reduce the pressure, a temperature controller 4, a sensor 5, and an electric valve 6 are used to slightly reduce the pressure. Create low-pressure steam and reduce the pressure in the distributor 7 to 0.05 kg/-, i.e. 10
Maintain at 2-103°C. A conduit 9 for supplying air into the bottle 8 is taken out from the distributor 7, and a solenoid valve 10 is installed near the distributor.
is installed, and the air supply time is set to an arbitrary time using the timer 11.
The device is designed to be able to insert the amount of steam, and since the temperature controller 4 cannot cope with fluctuations in the amount of steam, a solenoid valve 12 is installed in parallel with the electric valve 6 and operates at the same time as the solenoid valve 10 after the distributor 7. This prevents pressure drop in the distributor 7. In addition, when the use of steam is interrupted, there is a pressure drop due to heat radiation from the distributor and conduit, but this is due to the temperature controller 4.
functions to maintain a constant temperature. Distributor 7
The conduit 9 coming out of the
While the solenoid valve 10 is stopped, air is not supplied, so the conduit after the solenoid valve is cooled, and the steam in the conduit 9 becomes water droplets, and water droplets are inserted the next time air is supplied. It is made to penetrate through the air so that it retains heat and does not cool down even when air is not supplied.

導管9は多数(たとえば12本)同時に使用するので分
配器3は平均に蒸気を送るための多量の容量を保有する
。又導管9の取出しは分配器7の上部から取出し、湿り
蒸気及び水滴を送気しない様に分配器7下部にはドレン
の排出管を取付はトラップにてすみやかに排出する。
Since a large number of conduits 9 (for example 12) are used simultaneously, the distributor 3 has a large capacity for delivering steam evenly. Further, the conduit 9 is taken out from the upper part of the distributor 7, and a drain discharge pipe is installed at the lower part of the distributor 7 so as not to send in humid steam and water droplets, and the drain is quickly discharged using a trap.

ビン中に送る蒸気は一定時間に同量を送るために分配器
7後の電磁弁10及び電磁弁10後の導管9の長さは全
て同長とする。ビン中に送る蒸気は微低圧でないオガ屑
をはき出すこともあるのでこの調節は減圧弁2及び温度
調節器4により自在にすることが可能である。
The lengths of the solenoid valve 10 after the distributor 7 and the conduit 9 after the solenoid valve 10 are all made the same length so that the same amount of steam is sent into the bottle in a fixed time. Since the steam sent into the bottle may expel sawdust that is not at very low pressure, this adjustment can be made freely by the pressure reducing valve 2 and the temperature regulator 4.

また第2図に示すようにビン8中に蒸気を送気する機械
的な構造は連続機の場合は、コンベアー14により一定
方向にビン8が移動し、送気導管9の下部で停止すると
同時に導管9がビン8中に ゛入り、一定時間の送気終
了後、導管9は上部へ上がるとビン9はコンベア14に
より移動する方法であり、手動式の場合は導管9は定位
置に固定し、ビン8が下部より導管に向かって上がり一
定時間送気するものである。
In addition, as shown in FIG. 2, the mechanical structure for supplying steam into the bin 8 is that in the case of a continuous machine, the bin 8 is moved in a fixed direction by a conveyor 14, and is stopped at the bottom of the air supply conduit 9 at the same time. The conduit 9 enters the bottle 8, and after a certain period of air supply, the conduit 9 rises to the top and the bottle 9 is moved by the conveyor 14. In the manual type, the conduit 9 is fixed in a fixed position. , the bottle 8 rises from the bottom toward the conduit to supply air for a certain period of time.

以上述べた如く本発明にあっては、ビン等の容器中に材
料(オガ屑及び米−ぬか)を入れた後、ビン中の空気を
排出するために蒸気を挿入するが同時に殺菌物の温度を
大気圧下の最高温度まで上昇させることによって完全脱
気できる事を応用したものであり、脱気後はすみやかに
開口部を閉じそのままの保温庫へ入れこのまま保護する
ことによってビンの中を湿熱による殺菌を継続するもの
である。加熱温度以上に加温する場合は圧力容器を使用
し加圧することにより高温加熱を行うことができる。
As described above, in the present invention, after putting materials (sawdust and rice bran) into a container such as a bottle, steam is inserted to exhaust the air in the bottle, but at the same time the temperature of the sterilized material is This technology takes advantage of the fact that complete deaeration can be achieved by raising the bottle to the highest temperature under atmospheric pressure.After deaeration, the opening is immediately closed and the bottle is placed in a heat insulating chamber to protect it, thereby creating a moist heat inside the bottle. This will continue sterilization. When heating to a temperature higher than the heating temperature, high-temperature heating can be achieved by applying pressure using a pressure vessel.

尚、この場合ビン容器内を一度加熱脱気したものは冷却
された場合にビン中は真空状態が起こり、外部の空気を
吸込みこの時点で雑菌が混入するので、冷却されないよ
うすみやかに保温又は加温する必要がある。
In this case, once the inside of the bottle is heated and degassed, a vacuum state will occur inside the bottle when it is cooled, and outside air will be sucked in and bacteria will be mixed in. Therefore, it should be kept warm or heated immediately to prevent it from cooling. It needs to be warmed up.

本実施例にっては保温庫に対する保温は過熱空気で行う
が、保温庫内を過熱空気と蒸気で加温する鳩麦は1立方
米の対比で考えると空気では0.21Kcal/3℃で
あり蒸気では0.58Kcal /3℃と空気の方が約
173以下の熱量で条件を満たすことができ、又扉の開
放による逃げの場合も蒸気の方が軽いために早く逃げる
。(高温、高圧になればなる程、蒸気の逃げは早くなる
。)一方空気の場合は温度差の移動のみであるから、比
較的庫内の温度変化が少ない。すなわち保温庫のエネル
ギーロスの問題にあっても、熱伝達率では蒸気の方が恢
群によい為に保温庫外壁への熱伝導がよく放熱も多いが
空気の場合は熱伝導が悪く、外壁への熱伝導も悪いので
放熱も少ない。さらに冷却方法については、乾熱の場合
は空気の収縮のみであるから自然放冷でも特に問題はな
いが湿熱殺菌の場合は、ビン中の昇温でもふれたが、特
に放冷する場合、ビン中の蒸気は凝縮するので極端な真
空状態を起こし、ビンを密閉した状態で冷却されると内
容物は勿論、一般的なポリ容器では極端に変型する。こ
のために殺菌終了後はすみやかに無菌室でビンの開放を
行い冷却する必要がある。この場合でも無菌空気の挿入
により殺菌後の処理により均一化、安定性を増大するこ
とができる。
In this example, the heat insulating storage is carried out using superheated air, but when considering the comparison of 1 cubic meter of pigeon wheat in which the inside of the heating storage is heated with superheated air and steam, air is 0.21 Kcal/3°C. Steam can meet the requirements with a calorific value of 0.58 Kcal/3°C, which is about 173 degrees or less, and even when the door is opened, steam escapes faster because it is lighter. (The higher the temperature and pressure, the faster the steam escapes.) On the other hand, in the case of air, only the temperature difference moves, so there is relatively little temperature change inside the refrigerator. In other words, when it comes to the problem of energy loss in thermal storage, steam has a better heat transfer rate, so it conducts heat to the outer wall of the insulation storage well and radiates a lot of heat, but air has poor heat conduction and Because the heat conduction is poor, there is also little heat dissipation. Furthermore, regarding the cooling method, in the case of dry heat sterilization, there is no particular problem with natural cooling as it only involves the contraction of air, but in the case of moist heat sterilization, the temperature inside the bottle may rise, but especially when cooling the bottle, there is no particular problem. The steam inside condenses, creating an extreme vacuum, and when the bottle is cooled in a sealed state, the contents, as well as a typical plastic container, are extremely deformed. For this reason, after sterilization, the bottles must be opened and cooled in a sterile room immediately. Even in this case, uniformity and stability can be increased by post-sterilization treatment by inserting sterile air.

(本発明の効果) しかして本発明によれば、従来湿熱と考えていた殺菌方
法は実は乾熱殺菌であり、好適な殺菌効果を得ることは
困難であったが、本発明によれば完全な湿熱殺菌となっ
たので殺菌効果が向上した。
(Effects of the present invention) However, according to the present invention, the sterilization method conventionally thought to be moist heat is actually dry heat sterilization, and it has been difficult to obtain a suitable sterilization effect, but according to the present invention, it is completely The sterilization effect has been improved due to the moist heat sterilization.

これとあいまって従来2時間から4時間も殺菌していた
ものが10分〜40分で充分な殺菌効果を上げることが
でき、作業能率の向上と省エネルギーに多大の効果があ
る。
Coupled with this, a sufficient sterilization effect can be achieved in 10 to 40 minutes, whereas conventional sterilization took 2 to 4 hours, and this has a great effect on improving work efficiency and saving energy.

又設備的にも従来は容器内をすべて湿熱にしていたがビ
ン中を100℃内で殺菌する場合は、容器内は乾熱でよ
く、100℃以上の場合は圧力容器で湿熱を使用するが
、すでに100℃以内ではビン中の温度は昇温はしてい
るので容器内は保温するための熱量で充分でありエネル
ギーは極めて少量でよく、圧力容器の湿熱にあってもビ
ン中に与えるエネルギーは、従来の冷却状態から過温す
る場合に比べて、すでに100℃位まで昇温しであるの
で100℃以上の10〜20℃の加温でよく、その後は
保温状態を維持すればよく、従来圧力装置内及びビン中
の空気を排出するだめの逃がし弁の開放は一切不用であ
る。
In terms of equipment, conventionally everything inside the container was heated using moist heat, but if the inside of the bottle is to be sterilized at 100°C, dry heat can be used inside the container, but if the temperature is over 100°C, moist heat is used in a pressure vessel. , the temperature inside the bottle is already rising within 100℃, so the amount of heat needed to keep the inside of the container warm is sufficient, and only a very small amount of energy is required. Compared to the case of overheating from a conventional cooling state, the temperature has already increased to about 100°C, so heating to 10 to 20°C above 100°C is sufficient, and after that, it is sufficient to maintain the heat retention state. There is no need to open any relief valves for discharging the air in conventional pressure devices and bottles.

また加水の方法についても、従来は材料をビン詰する以
前に相当量の加水を行い、したが;て殺菌中には材料表
面の水分を空気が奪い、膨張した空気は一部排出される
ので水分量は減少の傾向にあった。また本来原材料が含
水していた水分とビン詰直前の水分では、含水が平均加
せず殺菌状態はもとより一定化せず栽培に当たっても均
一化が計れない原因ともなっていたが、本発明にあって
は、ビン詰以前ではほとんど加水は行われず、蒸気を入
れることによって全重量の10%〜15%の加水は簡単
に加水することができ、又送気時間の延長によ増量する
ことは自在であり、又蒸煮中に加水するので材料の含水
状態が一定化し、殺菌状態も均一化し均一な栽培が可能
となった。
Regarding the method of adding water, conventionally a considerable amount of water was added to the material before bottling it; however, during sterilization, air took away the moisture from the surface of the material, and some of the expanded air was expelled. The water content tended to decrease. In addition, between the moisture originally contained in the raw materials and the moisture immediately before bottling, the moisture content was not averaged, and the sterilization state was not constant, which caused it to be impossible to achieve uniformity during cultivation. Before bottling, almost no water is added, and by adding steam, 10% to 15% of the total weight can be easily added, and the amount can be increased by extending the air supply time. Also, since water is added during steaming, the water content of the material becomes constant, the sterilization state is also uniform, and uniform cultivation is possible.

以上述べた如く、本発明のきのこ栽培方法によれば、効
率よく充分な湿熱殺菌を行うことができるため、雑菌等
が入りこみ繁殖する余地はなく省エネルギーの下、経済
的で好適なきのこ栽培を行うことが可能となった。
As described above, according to the mushroom cultivation method of the present invention, it is possible to carry out efficient and sufficient moist heat sterilization, so there is no room for bacteria to enter and multiply, and mushroom cultivation can be carried out economically and favorably while saving energy. It became possible.

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

第1図は本発明のきのこ栽培方法に使用されるビン等の
容器に対する湿熱殺菌工程を示す説明図、第2図は本発
明のきのこ栽培方法に使用されるビン等の容器に対する
他の実施例に係る湿熱殺菌工程を示す概略側面図である
。 1・・・セパレーター  2・・・減圧弁3・・・蒸気
分配器  4・・・温度調節器  5・・・センサー 
 6・・・電動バルブ  7・・・分配器  8・・・
ビン   9・・・導管10・・・電磁弁  11・・
・タイマー  12・・・電磁弁  13・・・蒸気室
  14・・・コンベアー
FIG. 1 is an explanatory diagram showing a moist heat sterilization process for containers such as bottles used in the mushroom cultivation method of the present invention, and FIG. 2 is another example of containers such as bottles used in the mushroom cultivation method of the present invention. It is a schematic side view showing the wet heat sterilization process concerning. 1... Separator 2... Pressure reducing valve 3... Steam distributor 4... Temperature controller 5... Sensor
6...Electric valve 7...Distributor 8...
Bottle 9... Conduit 10... Solenoid valve 11...
・Timer 12...Solenoid valve 13...Steam room 14...Conveyor

Claims (1)

【特許請求の範囲】[Claims] ビン等の容器によるきのこ栽培方法において、容器中に
オガ屑及び米ぬか等の所要材料を収納した後、前記容器
中には蒸気を挿入し所要温度まで上昇させることにより
完全脱気し、脱気後は容器の開口部を閉じ保温庫に入れ
、これを保護することにより容器内の湿熱殺菌を継続せ
しめ、その後殖菌し芽出し栽培を行うことを特徴とする
きのこ栽培方法。
In a mushroom cultivation method using a container such as a bottle, after storing necessary materials such as sawdust and rice bran in the container, steam is inserted into the container and the temperature is raised to the required temperature to completely degas the container. This method of cultivating mushrooms is characterized by closing the opening of the container, placing it in a heat-retaining chamber, and protecting the container to continue moist heat sterilization inside the container, after which the bacteria propagate and sprout.
JP60017607A 1985-01-31 1985-01-31 Culture of mushroom Granted JPS61177928A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60017607A JPS61177928A (en) 1985-01-31 1985-01-31 Culture of mushroom

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60017607A JPS61177928A (en) 1985-01-31 1985-01-31 Culture of mushroom

Publications (2)

Publication Number Publication Date
JPS61177928A true JPS61177928A (en) 1986-08-09
JPH0217129B2 JPH0217129B2 (en) 1990-04-19

Family

ID=11948569

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60017607A Granted JPS61177928A (en) 1985-01-31 1985-01-31 Culture of mushroom

Country Status (1)

Country Link
JP (1) JPS61177928A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5221733A (en) * 1991-02-22 1993-06-22 Donlar Corporation Manufacture of polyaspartic acids

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5221733A (en) * 1991-02-22 1993-06-22 Donlar Corporation Manufacture of polyaspartic acids

Also Published As

Publication number Publication date
JPH0217129B2 (en) 1990-04-19

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