JPH01146991A - Pyrolyzer of lumber and other plant material - Google Patents
Pyrolyzer of lumber and other plant materialInfo
- Publication number
- JPH01146991A JPH01146991A JP62307244A JP30724487A JPH01146991A JP H01146991 A JPH01146991 A JP H01146991A JP 62307244 A JP62307244 A JP 62307244A JP 30724487 A JP30724487 A JP 30724487A JP H01146991 A JPH01146991 A JP H01146991A
- Authority
- JP
- Japan
- Prior art keywords
- steam
- heating
- wood
- indirect heating
- pyrolysis
- 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
Links
- 239000000463 material Substances 0.000 title abstract description 17
- 238000010438 heat treatment Methods 0.000 claims abstract description 76
- 238000000197 pyrolysis Methods 0.000 claims abstract description 19
- 239000000567 combustion gas Substances 0.000 claims abstract description 9
- 239000002023 wood Substances 0.000 claims description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 22
- 241001251054 Formica truncorum Species 0.000 claims description 6
- 238000005338 heat storage Methods 0.000 claims description 5
- 238000000354 decomposition reaction Methods 0.000 claims description 3
- 239000003973 paint Substances 0.000 claims description 2
- 230000002093 peripheral effect Effects 0.000 claims description 2
- 239000000341 volatile oil Substances 0.000 abstract description 25
- 230000000694 effects Effects 0.000 abstract description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 6
- 229910052799 carbon Inorganic materials 0.000 abstract 2
- 238000000034 method Methods 0.000 description 20
- 238000003763 carbonization Methods 0.000 description 12
- 241000196324 Embryophyta Species 0.000 description 11
- 150000003839 salts Chemical class 0.000 description 10
- 238000005979 thermal decomposition reaction Methods 0.000 description 9
- 238000001256 steam distillation Methods 0.000 description 8
- 241000218691 Cupressaceae Species 0.000 description 7
- 238000002485 combustion reaction Methods 0.000 description 6
- 239000003610 charcoal Substances 0.000 description 5
- 239000003921 oil Substances 0.000 description 5
- 239000010639 cypress oil Substances 0.000 description 4
- 235000021419 vinegar Nutrition 0.000 description 4
- 239000000052 vinegar Substances 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 238000007664 blowing Methods 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical group [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 210000000988 bone and bone Anatomy 0.000 description 2
- 239000011247 coating layer Substances 0.000 description 2
- 238000004925 denaturation Methods 0.000 description 2
- 230000036425 denaturation Effects 0.000 description 2
- 230000006698 induction Effects 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000002352 steam pyrolysis Methods 0.000 description 2
- 230000004913 activation Effects 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 210000002615 epidermis Anatomy 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 241000411851 herbal medicine Species 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 210000003491 skin Anatomy 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000013077 target material Substances 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Coke Industry (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Fats And Perfumes (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は水蒸気熱分解と乾溜による熱分解とが自動的
或いは任意に選択できる木材、植物の熱分解装置に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an apparatus for pyrolyzing wood and plants in which steam pyrolysis and pyrolysis by dry distillation can be automatically or arbitrarily selected.
従来、木材や植物から油成分を熱分解により溜出する方
法として水蒸気熱分解が周知である。例えば、■材料を
密閉容器内の水に浸し、密閉容器を直火又は蒸気等で加
熱する方法、■材料を炉内に設けた格子の上に積重ね、
格子の下側に入れた水を間接加熱する方法、■材料を入
れた密閉容器内にその底部より水蒸気を吹き込む方法が
ある。Steam pyrolysis is conventionally known as a method for distilling oil components from wood or plants by pyrolysis. For example, (1) immersing the materials in water in a sealed container and heating the sealed container with direct fire or steam; (2) stacking the materials on a grate in a furnace;
There are two methods: indirect heating of water placed under a grid, and (2) a method of blowing steam into a sealed container containing materials from the bottom.
これらの熱分解方法は直接又は間接的に水蒸気を吹き込
むことにより分離した精油は水蒸気と共に沸騰して溜出
するが、この漏出温度は精油成分の沸点よりはるかに低
いため、精油の分解変質を防止し、しかも大量生産にも
適する方法として一般に知られている。In these thermal decomposition methods, the separated essential oil is boiled and distilled together with the steam by directly or indirectly blowing steam into it, but since the leakage temperature is much lower than the boiling point of the essential oil components, decomposition and deterioration of the essential oil can be prevented. However, it is generally known as a method suitable for mass production.
しかしながら、上記方法にて得た精油の品質は良好であ
るが、蒸気による油成分の漏出重罪ち実収率が低いこと
、木材はチップ等に細断投入という面倒な工程を必要と
したこと、このようなチップ化し難い廃木材は投棄以外
になったことなど、各種の問題点があった。また、上記
方法を実施する生産業者の殆どが燃料として薪を用いる
零細産業であり、省エネ、大量生産には限界があった。However, although the quality of the essential oil obtained by the above method is good, the actual yield rate is low due to leakage of oil components due to steam, and the troublesome process of shredding the wood into chips etc. is required. There were various problems, including the fact that waste wood that is difficult to turn into chips had to be discarded. In addition, most of the producers implementing the above method are small-scale industries that use firewood as fuel, and there are limits to energy saving and mass production.
この発明は上記問題を解消するためのものであって、間
接加熱法により緩やかに、しかも均一に被熱分解物を収
容した密閉容器を加熱し、熱分解できる熱分解装置を提
供することを目的としている。また、他の目的は廃木材
を含め木材をチップ化することなく処理できる省力化や
効率化に優れた熱分解装置を提供すること、更に、他の
目的は夜間の無人乾留精油を行うことを可能にした熱分
解装置を提供すること、更に、他の目的は省エネや大量
生産性が期待できる熱分解装置を提供することにある。This invention is intended to solve the above problem, and an object of the present invention is to provide a pyrolysis device that can heat and pyrolyze a closed container containing a product to be pyrolyzed slowly and uniformly using an indirect heating method. It is said that Another purpose is to provide a pyrolysis device that is highly efficient and labor-saving, capable of processing wood, including waste wood, without turning it into chips.Another purpose is to provide a pyrolysis device that can process wood, including waste wood, without turning it into chips.Furthermore, another purpose is to provide a pyrolysis device that can process wood, including waste wood, without turning it into chips. Another objective is to provide a pyrolysis apparatus that can be expected to save energy and achieve mass productivity.
上記の目的を達成するため、この発明は、高速噴流バー
ナを有する下部室と燃焼ガスを旋回させる上部室とから
なる加熱炉と、内部に所定温度で溶融状態となる蓄熱性
のある熱媒体が封入され、外周面が前記加熱炉の上部室
内壁に一定の空隙を介して対面し、底面が下部室に面し
た凹状の間接加熱体と、被熱物分解が密閉収容でき、蓋
部に被熱分解による熱分解蒸気を取出す蒸気誘導管を有
し、前記間接加熱体の内面に一定の空隙を介して対面す
るように装入した装脱自在な密閉容器とを備え、前記間
接加熱体には熱電対及び複数個のヒーターを内蔵し、か
つ上部外周に蒸気発生缶帯を環状に付設し、前記密閉容
器の内底部に格子を設け、該格子の下側に前記蒸気発生
缶帯に接続手段を介して連通した蒸気噴出管を設けるこ
とによって、被熱分解物(例えば檜の小技や葉)を水蒸
気を熱媒体として一定の温度範囲(例えば、100°C
)以下で精油成分の沸点より遥かに低い温度で精油を溜
出させたり、乾留法に切変えることができるように構成
したものである。In order to achieve the above object, the present invention provides a heating furnace consisting of a lower chamber having a high-speed jet burner and an upper chamber in which combustion gas is swirled, and a heating medium having a heat storage property that becomes molten at a predetermined temperature inside. A concave indirect heating body whose outer peripheral surface faces the upper chamber wall of the heating furnace through a certain gap and whose bottom surface faces the lower chamber; a removable closed container having a steam guide pipe for extracting pyrolysis vapor from pyrolysis and facing the inner surface of the indirect heating body with a certain gap therebetween; has a built-in thermocouple and a plurality of heaters, and has a steam generating can band attached to the upper outer periphery in an annular shape, a grid is provided at the inner bottom of the sealed container, and the lower side of the grid is connected to the steam generating can band. By providing a steam jet pipe that communicates through a means, the material to be thermally decomposed (for example, Japanese cypress leaves) can be heated within a certain temperature range (for example, 100°C) using steam as a heat medium.
) or below, the essential oil can be distilled at a temperature far lower than the boiling point of the essential oil components, or the method can be switched to carbonization.
即ち、この発明は、■植物(葉)に含まれる精油及び木
材の表皮及び外木質部に含有される精油を蒸気にて熱変
成を避けながら溜出させる段階、■乾留により植物(葉
)に残留する成分及び木質部に存在する精油成分を木材
の水分を介して完全に精油として溜出させる段階、■更
に水分漏出した木材又は植物に対し熱分解としての乾留
法を進め、木材又は葉を炭化させ、木炭又は活生炭を製
造する段階を経て熱分解工程を終えることを可能にした
ものである。That is, this invention involves: (1) distilling essential oils contained in plants (leaves) and the epidermis and outer wood of wood using steam while avoiding thermal denaturation; and (2) distilling essential oils contained in plants (leaves) while avoiding thermal denaturation; A step of completely distilling the components and essential oil components present in the wood parts as essential oils through the moisture of the wood; ■Furthermore, proceed with the carbonization method as thermal decomposition for the wood or plants that leaked water, and carbonize the wood or leaves. , it is possible to complete the pyrolysis process through the stage of producing charcoal or live charcoal.
以下、この発明の一実施例を添付図面に基づいて説明す
る。An embodiment of the present invention will be described below with reference to the accompanying drawings.
図において、1は下部空間に高速噴流バーナ2を用いた
燃焼室(下部室)laを有し、上方に燃焼ガスを旋回さ
せる空間(上部室)lbを有する加熱炉である。ここに
高速噴流バーナ2を使用したのは加熱炉1をコンパクト
な炉体とする上に好適だからである。また、該加熱炉1
の燃焼室1a及び上部室1bの内壁面には遠赤外線塗料
を塗布した塗布層Rが形成されている。この塗布層Rは
高速噴流バーナ2により発生した熱を炉壁から内に向け
て輻射熱として放散させる機能と、炉体を通じて外部に
伝導される熱ロスを防止する機能を備えるものである。In the figure, reference numeral 1 denotes a heating furnace that has a combustion chamber (lower chamber) la using a high-speed jet burner 2 in the lower space, and a space (upper chamber) lb in which combustion gas is swirled upward. The high speed jet burner 2 is used here because it is suitable for making the heating furnace 1 into a compact furnace body. In addition, the heating furnace 1
A coating layer R coated with far-infrared paint is formed on the inner wall surfaces of the combustion chamber 1a and the upper chamber 1b. This coating layer R has the function of dissipating the heat generated by the high-speed jet burner 2 inward from the furnace wall as radiant heat, and the function of preventing heat loss conducted to the outside through the furnace body.
3は胴内部に所定温度(高温)にて溶融状態となる蓄熱
性のある熱媒体Sが封入された二重側構造の凹状の間接
加熱体で、該間接加熱体3はその外周面3aが前記加熱
炉1の上部室1bの内壁に一定の空隙4を介して対面す
ると共に、底面3bが下部室1aに面している。この蓄
熱性のある熱媒体Sとしては、例えば成分としてNaO
H+ XOHが70%以上、残りがNaC1,NazC
O,、、etcからなるソルト(中性塩浴、塊状−淡青
白色、比重1.9 /380°C又は1.81500”
C1使用範囲が250°c〜700°C)を封入して満
足できる。Reference numeral 3 denotes a concave indirect heating body with a double-sided structure in which a heat medium S having heat storage properties that becomes molten at a predetermined temperature (high temperature) is sealed inside the body. It faces the inner wall of the upper chamber 1b of the heating furnace 1 with a certain gap 4 in between, and the bottom surface 3b faces the lower chamber 1a. As the heat medium S having heat storage property, for example, NaO is used as a component.
H+ XOH is 70% or more, the rest is NaCl, NazC
Salt consisting of O,, etc. (neutral salt bath, lump-like pale bluish white, specific gravity 1.9/380°C or 1.81500"
C1 use range is 250°C to 700°C) and can be satisfied.
前記間接加熱体3には熱電対5及び複数個のヒーター6
が内蔵されている。この熱電対5は熱媒体(ツル1−)
Sの温度を測定して前記高速噴流バーナ2を制御するた
めのものである。また、ヒーター6は高温(250°C
以上)で溶解する上記ソルトの特質を活かし、熱媒体(
ソルト)Sを所定の温度に制御しつつ使用するものであ
る。即ち、ヒーター6による加熱温度を設定してタイマ
ーにより制御すれば夜間無人で熱分解を行わせることを
可能にしている。The indirect heating body 3 includes a thermocouple 5 and a plurality of heaters 6.
is built-in. This thermocouple 5 is a heat medium (temple 1-)
This is for controlling the high speed jet burner 2 by measuring the temperature of S. Also, the heater 6 is at a high temperature (250°C).
Taking advantage of the characteristics of the salt mentioned above, which dissolves in the heat medium (
Salt) S is used while controlling it to a predetermined temperature. That is, by setting the heating temperature by the heater 6 and controlling it by a timer, it is possible to carry out thermal decomposition unattended at night.
7は被熱分解物(例えば檜の小技や葉等)Aを密閉収容
できる密閉容器(カートリッジタンク)で、該密閉容器
7は前記間接加熱体3の凹部内面に一定の空隙8を介し
て対面するように装脱自在に装入した主部7aと、被熱
分解物Aの被熱分解による熱分解蒸気を取出すための蒸
気誘導管9を有する蓋部7bとからなる。この密閉容器
7の主部7aと間接加熱体3との間の空隙8は密閉容器
7を装脱するために必要なものであるが、空気層として
作用するため、主部7aの外周面に設けたフランジ10
にて間接加熱体3の上面を封緘し、熱を逃がさないよう
に考慮している。Reference numeral 7 denotes a closed container (cartridge tank) in which a material to be thermally decomposed (for example, Japanese cypress leaves, etc.) A can be hermetically housed. It consists of a main part 7a which is removably inserted so as to face each other, and a lid part 7b having a steam guide pipe 9 for taking out the pyrolysis steam generated by the thermal decomposition of the pyrolysed material A. The gap 8 between the main part 7a of the sealed container 7 and the indirect heating element 3 is necessary for loading and unloading the sealed container 7, but since it acts as an air layer, the gap 8 is provided flange 10
The upper surface of the indirect heating body 3 is sealed to prevent heat from escaping.
11は前記間接加熱体3の上部外周に環状に付設した蒸
気発生缶帯で、該蒸気発生缶!11は内部に水W1が注
入されている。この水W、は加熱炉1の燃焼室1aにて
発生した燃焼ガスおよび燃焼ガスで加熱される間接加熱
体3の伝熱で蒸気となる。この蒸気発生缶tR11で発
生した蒸気は逆止弁(図示せず)を内蔵した接続手段1
2を介して着脱自在に連繋した蒸気誘導管13を経て密
閉 。Reference numeral 11 denotes a steam generating can belt attached in an annular manner to the upper outer periphery of the indirect heating body 3, and the steam generating can! 11, water W1 is injected inside. This water W becomes steam by heat transfer through the combustion gas generated in the combustion chamber 1a of the heating furnace 1 and the indirect heating body 3 heated by the combustion gas. The steam generated in this steam generating can tR11 is transferred to a connecting means 1 having a built-in check valve (not shown).
It is sealed via a steam induction pipe 13 which is removably connected via 2.
容器7の主部7aの底部に導かれ、被熱分解物Aを載置
する格子14の下側に設けた蒸気放出管15から噴出さ
れるようになっている。この場合、格子14は密閉容器
7の主部7aの底部に一定量の水W2を収容できる空間
を作るためものである。The steam is guided to the bottom of the main part 7a of the container 7 and is ejected from a steam discharge pipe 15 provided below a grid 14 on which the pyrolyzable material A is placed. In this case, the grid 14 is used to create a space at the bottom of the main portion 7a of the closed container 7 that can accommodate a certain amount of water W2.
また、蒸気放出管15の蒸気噴出口15aは下向きにな
り、被熱分解物Aを収容した上部に均一に蒸気が充満で
きるようにしている。なお、前記逆止弁を内蔵した接続
手段12の部分には圧力計や安全弁等を付帯させておく
こともある。Further, the steam outlet 15a of the steam discharge pipe 15 is directed downward, so that the upper part containing the thermal decomposition material A can be uniformly filled with steam. In addition, a pressure gauge, a safety valve, etc. may be attached to the connecting means 12 containing the check valve.
なお、16は密閉容器7の蓋部7bの腕部が嵌合する開
閉ガイド杆、17は蓋部7bを主部7aに緊締する緊締
具である。Note that 16 is an opening/closing guide rod into which the arm of the lid 7b of the airtight container 7 fits, and 17 is a tightening tool for tightening the lid 7b to the main portion 7a.
上記実施例において、熱媒体の入った間接加熱体3は加
熱炉1の燃焼室1aに備えた高速噴流バーナ2の完全燃
焼により生じた燃焼ガスが加熱炉1の上部室1bと間接
加熱体3との隙間4を高速で流通し、逐次、加熱炉1の
燃焼ガス排出口3′に流れることにより底面及び外周全
面から均一的に加熱される。この場合、間接加熱体3の
各部位に加わる単位面積当りの熱エネルギー量にはバラ
ツキを生じるが、加えられた熱エネルギーは先ず熱媒体
に潜熱として蓄積され、この熱媒体内で均一になった後
、間接加熱体3の内側面へと発散されることとなるので
、密閉容器7へは均一的な分布をもつ加熱エネルギーと
して伝達されることになる。即ち、間接加熱体3内の熱
媒体は早く所定の温度に達する(底部のみを加熱した場
合の172の時間でよい)。この熱媒体はその温度の上
昇により固体が250℃において溶融するソルトである
場合には間接加熱帯3を250〜450°Cの範囲内で
使用すると、その熱量を空気層を介して被熱分解物Aの
入った密閉容器7が所定の温度になるまで速やかに均一
に伝導する。従って、所定の被熱分解物を密閉容器7内
に収納してお(ことにより被熱分解物は一定の均一な品
質の精油を含んだ蒸気を生じ、該蒸気は蒸気誘導管9を
経て図示していない冷却器を通って精油と水と液化しな
いガスとに分解し、精油は油水分離器を経て油槽へ導か
れ、液化しないガスは例えば本装置に併設したプレヒー
タに装着した密閉容器を予熱するため、或いは他の熱交
換器等に再利用されるか、放出される。In the above embodiment, the indirect heating body 3 containing the heat medium is arranged so that the combustion gas generated by complete combustion of the high speed jet burner 2 provided in the combustion chamber 1a of the heating furnace 1 is transferred to the upper chamber 1b of the heating furnace 1 and the indirect heating body 3. It flows at high speed through the gap 4 between the heating furnace 1 and the combustion gas outlet 3' of the heating furnace 1, thereby uniformly heating the bottom surface and the entire outer periphery. In this case, the amount of thermal energy per unit area applied to each part of the indirect heating element 3 varies, but the applied thermal energy is first accumulated as latent heat in the heating medium and becomes uniform within this heating medium. Thereafter, the heat is radiated to the inner surface of the indirect heating body 3, so that it is transmitted to the closed container 7 as heating energy with a uniform distribution. That is, the heat medium in the indirect heating body 3 reaches the predetermined temperature quickly (it takes only 172 hours when only the bottom is heated). If this heating medium is a salt whose solid melts at 250°C due to the rise in temperature, if indirect heating zone 3 is used within the range of 250 to 450°C, the amount of heat will be transferred through the air layer to undergo thermal decomposition. The conduction is carried out quickly and uniformly until the closed container 7 containing the substance A reaches a predetermined temperature. Therefore, a predetermined thermally decomposed product is stored in a closed container 7 (thereby, the thermally decomposed product generates steam containing essential oil of a certain uniform quality, and the steam is passed through a steam guide pipe 9 to Passing through a cooler (not shown), it is decomposed into essential oil, water, and non-liquefied gas.The essential oil is led to an oil tank via an oil-water separator, and the non-liquefied gas is preheated, for example, in a sealed container attached to a preheater attached to this device. or recycled to other heat exchangers, etc., or discharged.
この場合において、被熱分解物Aは初期段階では水蒸気
蒸留、中期段階では自動的に水蒸気蒸留を経て乾留が行
われ、最終段階では乾溜だけにより処理される。これに
より目的の木材(間抜技)及び植物(葉)は所期の対象
である精油が任意の温度制御により自在に選択採取でき
得ると共に、残渣となる木材又は植物は木炭として或い
は水蒸気賦活により活性炭として再生できることとなり
、被熱分解物を一片の無駄もなく活用できるという多大
の効果を納め得る。In this case, the thermally decomposed product A is subjected to steam distillation in the initial stage, automatically undergoes steam distillation and carbonization in the middle stage, and is treated only by dry distillation in the final stage. As a result, the essential oil of the desired target wood (smart technique) and plant (leaf) can be freely selected and collected by arbitrary temperature control, and the wood or plant residue can be collected as charcoal or by steam activation. It can be recycled as activated carbon, which has the great effect of making it possible to utilize the thermally decomposed product without wasting any of it.
今、前記密閉容器7内に被熱分解物Aとして木材(檜の
小技)と、植物(檜の葉)が混合して収納されていると
する。上記高速噴流バーナ2の作動により、■先ず、間
接加熱体3が加熱され、その上部に設けた蒸気発生缶W
ll内の水W、が蒸気となって蒸気誘導管13を通し・
て密閉容器7内に導かれ、蒸気噴出管15から放出され
る。従って、密閉容器7内の被熱分解物のうち、植物で
ある桧の葉と木材の皮や木質部の外表から精油(檜オイ
ル)が溜出する。■この蒸気発生缶帯11内の水が全部
蒸気となり、密閉容器7内への吹き込みが終了する時期
には、該密閉容器7内の温度はtoo”cに近くなって
おり、底部の水W2も蒸発し、木材自身の熱分解が始ま
り、葉及び皮等の水分と共に精油を溜出する。■この精
油の主成分である檜オイルはその沸点が167°Cであ
るので、熱分解が進行するにつれて密閉容器7内の温度
が180°C前後になると、木質部の成分(セルローズ
等)は炭化して黒くなる。■さらに、密閉容器7内の温
度を250°C前後まで上げて、その温度を保つと、木
酢(Pyroligneous Liquor)が溜出
して炭化が完了する。■密閉容器7内の温度が200’
C前後になった時点には蒸気発生缶帯11内に再び適量
の水を注入して蒸気を発生させる。■前記■の如く木酢
が溜出して炭化が完了した時点で前記■にて発生した蒸
気を炭化木材(木炭)に供給し、水蒸気賦活を行うと、
その木炭は活性炭となる。以上の■〜■の熱分解完了ま
での時間には約240分を要する。Now, it is assumed that a mixture of wood (Japanese cypress) and plants (Japanese cypress leaves) are stored as the thermally decomposed material A in the airtight container 7. By the operation of the high-speed jet burner 2, the indirect heating element 3 is first heated, and the steam generating can W provided above the indirect heating element 3 is heated.
The water W in ll becomes steam and passes through the steam induction pipe 13.
The steam is guided into the closed container 7 and discharged from the steam jet pipe 15. Therefore, among the materials to be thermally decomposed in the airtight container 7, essential oil (cypress oil) is distilled from the leaves of the Japanese cypress plant, the bark of the wood, and the outer surface of the woody part. ■ By the time all the water in this steam generating can zone 11 has turned into steam and the blowing into the sealed container 7 has ended, the temperature inside the sealed container 7 is close to too"c, and the water W2 at the bottom The wood itself evaporates, and the wood itself begins to decompose, distilling the essential oil along with the water in the leaves, skin, etc. ■ Cypress oil, the main component of this essential oil, has a boiling point of 167°C, so thermal decomposition progresses. As the temperature inside the airtight container 7 increases to around 180°C, the components of the wood (cellulose, etc.) carbonize and turn black.■Furthermore, the temperature inside the airtight container 7 is raised to around 250°C. When the temperature is maintained, the pyroligneous liquor will distill out and carbonization will be completed. ■ The temperature inside the airtight container 7 will be 200'.
When the temperature reaches around C, an appropriate amount of water is again injected into the steam generating can zone 11 to generate steam. ■When the wood vinegar is distilled out and carbonization is completed as in (■) above, the steam generated in (■) is supplied to the carbonized wood (charcoal) to activate the steam,
The charcoal becomes activated carbon. It takes about 240 minutes to complete the thermal decomposition in steps (1) to (2) above.
このようにして処理を終了した後は、適宜手段により密
閉容器7を間接加熱体3内から取外すとともに、炉外の
作業し易い場所にて密閉容器7に次回の被熱分解物を充
填し、再び密閉容器7を間接加熱体3の内部に装着する
。この密閉容器7の取出・装着の間に多少時間が掛かっ
ても前記熱媒体は蓄熱効果が働くので、間接加熱体3の
温度低下を阻止する。従って、次回の熱分解ガスの発生
に要する加熱エネルギーの量を著しく節約することが可
能となる。After completing the treatment in this way, the sealed container 7 is removed from the indirect heating body 3 by appropriate means, and the sealed container 7 is filled with the next thermal decomposition material in an easily accessible place outside the furnace. The airtight container 7 is mounted inside the indirect heating body 3 again. Even if it takes some time to take out and install the airtight container 7, the heat medium has a heat storage effect, so that the temperature of the indirect heating body 3 is prevented from decreasing. Therefore, it becomes possible to significantly save the amount of heating energy required for the next generation of pyrolysis gas.
また、予め複数個の密閉容器7を用意し、交換的に間接
加熱体3に装着する如くすれば、作業能率を著しく向上
させることができ、かつ、熱ロスの殆どない状態で加熱
処理を行うことが可能となる。In addition, by preparing a plurality of airtight containers 7 in advance and attaching them to the indirect heating element 3 in exchange, the work efficiency can be significantly improved, and the heat treatment can be performed with almost no heat loss. becomes possible.
さらに、熱源であるバーナ2から密閉容器7への加熱作
用を中間加熱体3を介して行うように構成しているので
、もし密閉容器7が損傷することにより内容物が漏れる
ことがあったとしても間接加熱体3により受けられるた
め作業の安全性を保つことが可能となるし、間接加熱体
3に損傷等の不測の事故が発生し、ソルトが漏れた場合
でも上記のソルトは爆発することなく単に燃焼するだけ
であるから安全である。Furthermore, since the structure is configured such that the heating effect from the burner 2, which is a heat source, to the closed container 7 is performed via the intermediate heating element 3, even if the contents leak due to damage to the closed container 7, It is possible to maintain the safety of work because the salt is received by the indirect heating element 3, and even if an unexpected accident such as damage to the indirect heating element 3 occurs and the salt leaks, the above-mentioned salt will not explode. It is safe because it simply burns.
次に具体例を、(1)水蒸気蒸溜法の場合と、(2)乾
留法の場合(初期水蒸気蒸留後乾留)とに分けて説明す
る。Next, specific examples will be explained separately for (1) the case of steam distillation and (2) the case of carbonization (carbonization after initial steam distillation).
(1)水蒸気蒸溜法の場合
容積が0.4nfの密閉容器7の主部7aの底部に30
fの水を注入後、格子14の上に、150kgの植物(
檜の葉)を収納し、蓋部7bを締めて密閉した後、内部
ソルトを溶解状態に加熱した中間加熱体3内に嵌入する
。しかる後、密閉容器を100°Cを保つように高速噴
流バーナ2を熱電対により温度制御しつつ加熱し、蒸気
発生缶9911内に注入した容量702の水を蒸気とし
、この蒸気の発生状況により更に水を逐次注入して蒸気
にし、逆止弁を介し密閉容器7内の格子下の蒸気放出管
15より放出させた処、中間加熱体3内に密閉容器7を
嵌入から180分で精油(檜オイル) 1.1ffi
を得た(木酢およびタール分は溜出しなかった)。(1) In the case of steam distillation, a
After injecting water of f, 150 kg of plants (
After storing the cypress leaves) and sealing the container by tightening the lid 7b, the container is inserted into the intermediate heating member 3 which has heated the internal salt to a molten state. Thereafter, the high-speed jet burner 2 is heated to maintain the temperature of the sealed container at 100°C while controlling the temperature with a thermocouple, and the water with a capacity of 702 injected into the steam generating can 9911 is turned into steam, and depending on the generation situation of this steam, Furthermore, water is successively injected to make steam, which is released from the steam release pipe 15 under the lattice in the closed container 7 via a check valve, and essential oil ( Hinoki oil) 1.1ffi
(wood vinegar and tar were not distilled out).
(2)乾留法の場合(初期水蒸気蒸留後乾留)容積が0
.4nfの密閉容器7の主部7aの底部に30ffiの
水を注入後、格子14の上に、150kgの木材(檜の
間材小技)を収納し、蓋部7bを締めて密閉した後、内
部ソルトを溶解状態に加熱した中間加熱体3内に嵌入す
る。しかる後、その中間加熱体3を密閉容器内が250
°Cに達するまで高速噴流バーナ2を断続的に加熱制御
すると、先ず、底部に注入されている301の水が蒸気
となって木材の皮及び木質部表部より精油を水蒸気熱分
解して溜出した後、木材の木質部に含まれる約70%の
水分が木質成分と檜オイルと共に蒸発し、乾留となり、
媒介蒸気が少ないので水分の少ない精油が溜出し、約2
40分にて250°Cに達した時点で木酢骨を溜出した
ので中止した。精油量は2.22であった。(2) In the case of carbonization method (carbonization after initial steam distillation) the volume is 0
.. After pouring 30ffi of water into the bottom of the main part 7a of the 4nf airtight container 7, 150 kg of wood (Japanese cypress spacing) was stored on the lattice 14, and the lid part 7b was tightened to seal it. It is inserted into the intermediate heating body 3 which has heated the internal salt to a molten state. After that, the intermediate heating body 3 is heated to a temperature of 250 mL in the closed container.
When the high-speed jet burner 2 is intermittently heated until the temperature reaches °C, the water injected into the bottom of 301 turns into steam, and the essential oil is steam pyrolyzed and distilled from the bark and surface of the wood. After that, approximately 70% of the water contained in the woody part of the wood evaporates together with the wood components and cypress oil, resulting in carbonization.
Because there is little vapor as a medium, essential oils with low water content are distilled out, and approximately 2.
When the temperature reached 250°C in 40 minutes, pyroligneous bones were distilled out, so the process was stopped. The amount of essential oil was 2.22.
なお、210°Cの時点では未だ木酢骨の臭がしなかっ
たので、この時点で中止すれば精油量は減少するが、木
酢臭は止め得るし、さらに加温すれば約300°Cでタ
ール分も溜出することが理論的に可能である。しかし目
的の檜オイル採油と外れるので行わなかった。Note that at 210°C, there was still no odor of wood vinegar bones, so if you stop heating at this point, the amount of essential oil will decrease, but you can stop the wood vinegar odor, and if you heat it further, it will become tarry at about 300°C. It is theoretically possible to distill off the fraction as well. However, this was not done as it would be inconsistent with the objective of extracting cypress oil.
なお、上記実施例では説明していないが、密閉容器7の
蓋部7bを液密に構成し、内部に冷却水を流入し、密閉
容器7内で発生した蒸気を冷却できるように構成するこ
ともある。即ち、このように構成することにより、水蒸
気蒸溜を行うに際して所定量の植物と蒸気を密閉容器内
に封入後、蒸気誘導管を閉じ、蓋部に冷却水を流入する
と、封入蒸気は蒸発→冷却して水滴になって降下→蒸発
を繰返し、植物の成分は蒸気を追加することなく抽出さ
れるようになり、漢方薬等の煮つめ液の製造に効果的に
活用できる。Although not explained in the above embodiments, the lid 7b of the hermetic container 7 may be configured to be liquid-tight so that cooling water can flow inside to cool the steam generated within the hermetic container 7. There is also. That is, with this configuration, when performing steam distillation, after sealing a predetermined amount of plants and steam in a sealed container, closing the steam guide pipe and flowing cooling water into the lid, the sealed steam evaporates and then cools. By repeating the process of falling and evaporating as water droplets, plant components can be extracted without adding steam, and can be effectively used in the production of boiled liquids for Chinese herbal medicines.
まjこ、そのような工程を経た後、冷却水を放流し、間
接加熱体の温度を上げ、かつ、蒸気誘導管9を開けば上
記実施例の作動にそのまま移行できるので支障はない。After passing through such a process, if the cooling water is discharged, the temperature of the indirect heating element is raised, and the steam guide pipe 9 is opened, the operation can be directly carried out as in the above embodiment, so there is no problem.
以上の如く、この発明は高速噴流バーナを有する下部室
と燃焼ガスを旋回させる上部室とからなる加熱炉と、内
部に所定温度で溶融状態となる蓄熱性のある熱媒体が封
入され、外周面が前記加熱炉の上部室内壁に一定の空隙
を介して対面し、底面が下部室に面した凹状の間接加熱
体と、被熱物分解が密閉収容でき、蓋部に被熱分解によ
る熱分解蒸気を取出す蒸気誘導管を有し、前記間接加熱
体の内面に一定の空隙を介して対面するように装入した
装脱自在な密閉容器とを備え、前記間接加熱体には熱電
対及び複数個のヒーターを内蔵し、かつ上部外周に蒸気
発生缶帯を環状に付設し、前記密閉容器の内底部に格子
を設け、該格子の下側に前記蒸気発生缶帯に接続手段を
介して連通した蒸気噴出管を設けたことを特徴としてい
るから、水蒸気蒸留と乾留とを兼ね得、目的の材料の成
分を合わせて材料を穏やか且つ均一に熱媒体を通じ加熱
し分解できると共に、目的材料により水蒸気蒸留も併用
出来るので品質の一定した精油を目的に合わせて採油で
きる。As described above, the present invention includes a heating furnace consisting of a lower chamber having a high-speed jet burner and an upper chamber in which combustion gas is swirled; The concave indirect heating body faces the upper chamber wall of the heating furnace through a certain gap, the bottom face faces the lower chamber, and the decomposition of the heat object can be hermetically housed. It has a steam guide pipe for extracting steam, and a removable sealed container inserted so as to face the inner surface of the indirect heating body through a certain gap, and the indirect heating body is equipped with a thermocouple and a plurality of thermocouples. a steam generating can band is attached to the outer periphery of the upper part in an annular manner, a lattice is provided at the inner bottom of the sealed container, and the lower side of the grid is connected to the steam generating can band through a connecting means. Because it is characterized by being equipped with a steam ejection tube, it can perform both steam distillation and carbonization, and can combine the components of the target material and gently and uniformly heat and decompose the material through a heating medium. Distillation can also be used in combination, so essential oils of consistent quality can be extracted for different purposes.
また、ヒーターにより少量の電力2 KW/H(0,4
n(の場合)という省エネルギーにより所定温度を維持
し、夜間、無人化乾留法を採用でき、採油率の向上が期
待できるという優れた効果を奏するものである。In addition, a small amount of electric power 2 KW/H (0,4
This has excellent effects in that it is possible to maintain a predetermined temperature by saving energy (in the case of n), to employ an unmanned carbonization method at night, and to expect an improvement in the oil extraction rate.
図はこの発明の一実施例を示すもので、第1図は正面断
面図、第2図は平面断面図、第3図は要部の拡大断面図
である。
1−・加熱炉
1a=燃焼室(下部室)
1b−・上部室
2−高速噴流バーナ
3−・中間加熱体
5−熱電対
6− ヒーター
7−密閉容器
1a−−・主部
7b・−蓋部
9.13−蒸気誘導管
11−・蒸気発生缶帯
12−・−接続手段
14−・格子
15−蒸気噴出管
第1図
第2図The drawings show an embodiment of the present invention; FIG. 1 is a front sectional view, FIG. 2 is a plan sectional view, and FIG. 3 is an enlarged sectional view of the main part. 1- Heating furnace 1a = Combustion chamber (lower chamber) 1b- Upper chamber 2- High speed jet burner 3- Intermediate heating body 5- Thermocouple 6- Heater 7- Sealed container 1a-- Main part 7b- Lid Part 9.13 - Steam guide pipe 11 - Steam generating can band 12 - Connection means 14 - Grid 15 - Steam jet pipe Fig. 1 Fig. 2
Claims (3)
させる上部室とからなる加熱炉と、内部に所定温度で溶
融状態となる蓄熱性のある熱媒体が封入され、外周面が
前記加熱炉の上部室内壁に一定の空隙を介して対面し、
底面が下部室に面した凹状の間接加熱体と、被熱物分解
が密閉収容でき、蓋部に被熱分解による熱分解蒸気を取
出す蒸気誘導管を有し、前記間接加熱体の内面に一定の
空隙を介して対面するように装入した装脱自在な密閉容
器とを備え、前記間接加熱体には熱電対及び複数個のヒ
ーターを内蔵し、かつ上部外周に蒸気発生缶帯を環状に
付設し、前記密閉容器の内底部に格子を設け、該格子の
下側に前記蒸気発生缶帯に接続手段を介して連通した蒸
気噴出管を設けたことを特徴とする木材、植物の熱分解
装置。(1) A heating furnace consisting of a lower chamber having a high-speed jet burner and an upper chamber in which combustion gas is swirled; a heating medium with heat storage properties that becomes molten at a predetermined temperature is sealed inside, and the outer peripheral surface of the heating furnace facing the upper indoor wall of the building through a certain gap,
A concave indirect heating body whose bottom face faces the lower chamber and a decomposing object to be heated can be hermetically housed, and a lid part has a steam guide pipe for taking out pyrolysis steam from the decomposition to be thermally decomposed. and a removable closed container charged so as to face each other through a gap, the indirect heating body has a built-in thermocouple and a plurality of heaters, and a steam generating can band is arranged in an annular shape around the upper outer periphery. The pyrolysis of wood and plants, characterized in that a lattice is provided at the inner bottom of the closed container, and a steam jet pipe is provided below the lattice and communicates with the steam generating can zone through a connecting means. Device.
のである特許請求の範囲第1項記載の木材、植物の熱分
解装置。(2) The apparatus for pyrolyzing wood and plants according to claim 1, wherein the heating furnace has an inner wall coated with far-infrared paint.
っている特許請求の範囲第1項記載の木材、植物の熱分
解装置。(3) The apparatus for pyrolyzing wood and plants according to claim 1, wherein the lid of the airtight container is capable of containing water.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62307244A JPH0647676B2 (en) | 1987-12-04 | 1987-12-04 | Pyrolysis equipment for wood and plants |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62307244A JPH0647676B2 (en) | 1987-12-04 | 1987-12-04 | Pyrolysis equipment for wood and plants |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01146991A true JPH01146991A (en) | 1989-06-08 |
JPH0647676B2 JPH0647676B2 (en) | 1994-06-22 |
Family
ID=17966771
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62307244A Expired - Lifetime JPH0647676B2 (en) | 1987-12-04 | 1987-12-04 | Pyrolysis equipment for wood and plants |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0647676B2 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002036711A1 (en) * | 2000-10-27 | 2002-05-10 | Yoshinobu Nitta | Heating furnace |
JP2006056232A (en) * | 2004-08-20 | 2006-03-02 | Damyangkun | Manufacturing device of bamboo bitumen and its manufacturing method |
JP2006328304A (en) * | 2005-05-30 | 2006-12-07 | Koichi Nakamura | Extraction method of plant tissue components |
JP2008093831A (en) * | 2006-10-05 | 2008-04-24 | M & F Technology Co Ltd | Injection molding resin, its manufacturing method, molding and extraction method of acetic acid component |
JP4874505B2 (en) * | 2000-10-27 | 2012-02-15 | 善信 新田 | heating furnace |
CZ309264B6 (en) * | 2021-02-10 | 2022-06-29 | THEODOR DESIGN, s.r.o | Method of thermal decomposition and the equipment for thermal decomposition |
-
1987
- 1987-12-04 JP JP62307244A patent/JPH0647676B2/en not_active Expired - Lifetime
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002036711A1 (en) * | 2000-10-27 | 2002-05-10 | Yoshinobu Nitta | Heating furnace |
JP4874505B2 (en) * | 2000-10-27 | 2012-02-15 | 善信 新田 | heating furnace |
JP2006056232A (en) * | 2004-08-20 | 2006-03-02 | Damyangkun | Manufacturing device of bamboo bitumen and its manufacturing method |
JP2006328304A (en) * | 2005-05-30 | 2006-12-07 | Koichi Nakamura | Extraction method of plant tissue components |
JP2008093831A (en) * | 2006-10-05 | 2008-04-24 | M & F Technology Co Ltd | Injection molding resin, its manufacturing method, molding and extraction method of acetic acid component |
CZ309264B6 (en) * | 2021-02-10 | 2022-06-29 | THEODOR DESIGN, s.r.o | Method of thermal decomposition and the equipment for thermal decomposition |
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