JPS607923A - Apparatus for deodorizing odorous gas by soil - Google Patents

Apparatus for deodorizing odorous gas by soil

Info

Publication number
JPS607923A
JPS607923A JP58115627A JP11562783A JPS607923A JP S607923 A JPS607923 A JP S607923A JP 58115627 A JP58115627 A JP 58115627A JP 11562783 A JP11562783 A JP 11562783A JP S607923 A JPS607923 A JP S607923A
Authority
JP
Japan
Prior art keywords
soil
gas
layer
suction blower
blower
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.)
Pending
Application number
JP58115627A
Other languages
Japanese (ja)
Inventor
Hiroshi Etani
恵谷 浩
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.)
Japan Steel Works Ltd
Original Assignee
Japan Steel Works Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Japan Steel Works Ltd filed Critical Japan Steel Works Ltd
Priority to JP58115627A priority Critical patent/JPS607923A/en
Publication of JPS607923A publication Critical patent/JPS607923A/en
Pending legal-status Critical Current

Links

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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Abstract

PURPOSE:To dispense with a heating apparatus for heating an odorous gas by insulating a blower and a duct for sucking the odorous gas with a heat insulating material, and heating the odorous gas with the heat generated from the operation of the suction blower. CONSTITUTION:A suction blower 7 is installed in an insulated chamber 13 constructed of a heat insulating material 12, and a duct 14 is insulated with a heat insulating material 12'. An odorous gas 10 is discharged into a cobblestone layer 3 from discharge ports 5 of a gas pipe 6 through the suction blower 7 and the duct 14. The odorous gas 10 is heated with the heat generated from the operation of the suction blower 7, dispersed while passing through the cobblestone layer 3 and a gravel layer 2, deodorized by a soil layer 1, and discharged into the atmosphere from the surface of the soil layer 1.

Description

【発明の詳細な説明】 本発明は、例えば都市ごみ堆肥化処理プラントで発生し
た悪臭ガスを、特に寒冷地においても、土壌中の微生物
を利用して脱臭することができる悪臭ガスの土壌による
脱臭装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides soil-based deodorization of malodorous gases, which can deodorize malodorous gases generated, for example, in municipal waste composting plants, using microorganisms in the soil, especially in cold regions. It is related to the device.

悪臭ガスの処理には、燃焼法、薬液洗浄法、活性炭吸着
法、イオン交換樹脂法、オゾン酸化法、マスキング法な
どあるが、近年都市とみあるいは家畜糞の堆肥化処理プ
ラント、畜肉処理廃棄物処理プラントなどから発生する
悪臭ガスの脱臭に(I:l:、土壌による脱臭法が行わ
れている。
There are combustion methods, chemical cleaning methods, activated carbon adsorption methods, ion exchange resin methods, ozone oxidation methods, masking methods, etc. to treat foul-smelling gases, but in recent years cities have started to use composting plants for livestock manure, livestock waste processing plants, etc. The soil-based deodorization method is used to deodorize foul-smelling gases generated from plants, etc.

これは、砂利などで形成した下層の上に、黒ボク土、畑
表土などの土壌あるいは堆肥を積層したものであって、
土壌中の土壌成分と悪臭物質との化学的中和反応あるい
は土壌中の細歯r’jどの微生物の分解作用で脱臭処理
をするものである。
This is a layer of soil such as black soil, field topsoil, or compost on top of a lower layer of gravel, etc.
Deodorizing treatment is performed through a chemical neutralization reaction between soil components and malodorous substances in the soil, or through the decomposition action of microorganisms such as microorganisms in the soil.

ところが、寒冷地においては、土壌の温度が約5 C以
下になると、微生物が休眠状態とナリ、微生物による悪
臭物質の分解作用が殆んどなくなるのス冬期では脱臭性
能が低下してし寸う。
However, in cold regions, when the soil temperature drops below about 5 degrees Celsius, the microorganisms become dormant and their ability to decompose malodorous substances almost disappears. .

まだ外気の温度が約−300となる極寒冷期には土壌か
凍結してその装置の運転そのものが出来なくなる、とい
うのが現状である。
The current situation is that during the extremely cold season, when the outside air temperature is about -300 degrees Celsius, the soil freezes and the equipment cannot operate.

本発明は、このようt点に鑑みて開発したものであって
、寒冷地においても、土壌の温度を、極めて簡単な手段
で、微生物の悪臭物質の分解能力を低下しない程度に保
持して、脱臭性能を持続せしめた悪臭ガスの土壌Wよる
脱臭装置を一供せんとするものである。
The present invention was developed in view of the above point t, and it maintains soil temperature by extremely simple means to a level that does not reduce the ability of microorganisms to decompose malodorous substances, even in cold regions. The purpose is to provide a deodorizing device using soil W for foul-smelling gas that maintains deodorizing performance.

すなわちその要旨とするところは、 保温材をもって形成した保温室内に吸引プロワを設置し
、吸引プロワには、同ブロワの吸引運転により発生した
熱で加熱された悪臭ガスを導出するダクト配管を連設し
、ダクト配管は保温材をもって保温するとともに、これ
に、多数の排出孔を有するガス導管を接続し、ガス導管
は玉石層中に埋設するとともに、同層の上には砂利層を
、さらにその上には土壌層を積層した悪臭ガスの土壌に
よる脱臭装置Jある。
In other words, the gist is that a suction blower is installed in an insulated chamber made of heat insulating material, and a duct piping is connected to the suction blower to draw out the malodorous gas heated by the heat generated by the blower's suction operation. The duct piping is insulated with heat insulating material, and a gas pipe with many exhaust holes is connected to it.The gas pipe is buried in a cobblestone layer, and a gravel layer is placed on top of the cobblestone layer. Above is a soil-based deodorizing device J for foul-smelling gas, which is made up of layers of soil.

その構成を図示のものについて説明する。The configuration shown in the figure will be explained.

地1面(8)に→屈削孔(9)を湘ね、その四周をコン
クリートブロック(4)(4’)(4”)(4’)で囲
う、同ブロック(4’)(a’)(4′’)(4’)は
四角形に限らず多角形、円J杉でもよい。
Drill a hole (9) in the ground (8) and surround it with concrete blocks (4) (4') (4'') (4'). ) (4'') (4') is not limited to a quadrangle, but may be a polygon or a circle J cedar.

(3)は掘削孔(9)内において最下層に敷かれた玉石
層、(2)はその上側に敷かれた砂利層、(1)は最上
層の土壌層である。
(3) is the cobblestone layer laid at the bottom in the excavation hole (9), (2) is the gravel layer laid above it, and (1) is the top soil layer.

玉石層(3)にはガス排出孔(5)余有する導管(6)
を埋設中る。
The cobblestone layer (3) has a gas discharge hole (5) and a conduit (6).
is being buried.

一方、(13)は保温室であってその中に吸引プロワ(
1)全設置する11(14’)は吸引プロワ(1)によ
り吸引された悪臭ガス(lo)f導出するダクト配管で
吸引プロワ(−1)に連設し、ダクト配管(14”l 
i前記ガス導管(6)に接続する。
On the other hand, (13) is a storage room with a suction blower (
1) Completely installed 11 (14') is a duct piping that brings out the malodorous gas (lo) f sucked by the suction blower (1), and is connected to the suction blower (-1), and the duct piping (14"l)
i Connect to the gas conduit (6).

(12)は保温室(13)を形成する保温材、(12”
)はダクト配管(14)の保温材を示す。
(12) is a heat insulating material forming an insulating room (13), (12"
) indicates the heat insulating material of the duct pipe (14).

各保温材(12)(12’ )は、石綿保温材、岩綿保
温相、鉱ミ謬綿保温月、ガラス繊維保温材、珪藻土保温
相などであって、その厚さは悪臭ガス自身の温度と周囲
の空気の温度力Sら定められる。
Each insulation material (12) (12') is an asbestos insulation material, a rock wool insulation phase, an ore cotton insulation phase, a glass fiber insulation material, a diatomaceous earth insulation phase, etc., and its thickness is determined by the temperature of the malodorous gas itself. and the temperature force S of the surrounding air.

(11)は脱臭がなされた無臭ガスを示す。(11) indicates odorless gas that has been deodorized.

その作用を説明する。The effect will be explained.

今、都市ごみ堆肥化処理プラントにこれを設置した場合
について説明すると、同プラントより発生する悪臭ガス
(10)は吸引プロワ(7)よりダクト配管(14)を
経てガス導管(6)へ導かれ、その排出孔(5)より玉
石層(3)中に排出されるが、この場合、吸引プロワ(
7)は保温室(13)中に設置され、タリト配管(14
)は保温材(12′)で保温されている。そして悪臭ガ
ス(10) Rブロワ(7)の吸引運転自体で発生する
熱量により加熱される。したがって同ガス(1o)は、
寒冷地の場合でも、ブロワ(7)の出口で約30〜50
″Cの高温となっているし、またガス導管(6)のガス
排出孔(5)より玉石層(3)中に排出する温度は、約
20〜40 Cである。
Now, to explain the case where this is installed in a municipal waste composting plant, the malodorous gas (10) generated from the plant is guided from the suction blower (7) to the gas pipe (6) via the duct pipe (14). is discharged from its discharge hole (5) into the cobblestone layer (3), but in this case, the suction blower (
7) is installed in the insulating room (13), and the Talito piping (14)
) is kept warm by a heat insulating material (12'). The malodorous gas (10) is heated by the amount of heat generated during the suction operation of the R blower (7) itself. Therefore, the same gas (1o) is
Even in cold regions, the output of the blower (7) is about 30 to 50
The temperature at which the gas is discharged from the gas discharge hole (5) of the gas conduit (6) into the cobblestone layer (3) is approximately 20 to 40C.

玉石層(3)中に排出されたこの悪臭ガス(1o)は、
その上層の砂利層(2)中を通過する間に分散され土壌
層(1)に達する。
This foul-smelling gas (1o) discharged into the cobblestone layer (3) is
While passing through the upper gravel layer (2), it is dispersed and reaches the soil layer (1).

土壌層(1)中で分散された悪臭ガス(1o)の見掛流
速、寸7!わち、土壌層(1)の中での悪臭ガス(1o
)の通気速度は3〜20 るである。
Apparent flow velocity of malodorous gas (1o) dispersed in soil layer (1), size 7! In other words, the malodorous gas (1o) in the soil layer (1)
) The ventilation rate is between 3 and 20 degrees.

この間、悪臭物質は土壌に吸着されて脱臭され、同層(
1)の表面から無臭ガス(11)となり大気中に放出さ
れる。
During this time, malodorous substances are adsorbed to the soil and deodorized, and the same layer (
From the surface of 1), it becomes an odorless gas (11) and is released into the atmosphere.

悪臭ガス(10)の温度は、前記のように、球冷地でも
、ガス排出孔(5)より玉石層(3)中に排出される所
で約20−40″Cであるので、土壌層(1)の温度は
約6〜18 0に維持され、これが約5″c以下に低下
することはない。
As mentioned above, the temperature of the foul-smelling gas (10) is about 20-40"C at the point where it is discharged from the gas discharge hole (5) into the cobblestone layer (3) even in a cold area, so it is The temperature of (1) is maintained at about 6-180C and it never drops below about 5"C.

/Lお、悪臭ガス(1o)を加熱するには、これを電気
ヒーター、庫油ヒーターな゛どに通すことも考えられる
が、装置の保温さえ適正になされれば吸引プロワ(′7
)自体で発生する熱量で充分加熱し得るので、このよう
な必要はない。
/L To heat the foul-smelling gas (1o), it is possible to pass it through an electric heater, storage oil heater, etc., but if the equipment is properly kept warm, a suction blower ('7
) This is not necessary since the amount of heat generated by itself can be sufficient for heating.

悪臭ガス(10)を分解する土壌中の微生物としては、
アンモニアを酸化して亜硝酸にする亜硝酸菌、亜硝酸を
酸化して硝酸にする硝酸菌、硫化水素、メチルメルカプ
タベ硫化メチルなどの硫化物を分解する硫化菌、lT酸
、プロピオン酸、酪酸、吉草酸などの低級脂肪酸を分解
する放線菌、tx′F酸を分解する訂酸菌および酵母な
どがあるが、これらの微生物の増殖可能な温度は約5〜
60.0の範囲であって約5 C以下では休眠状態とな
る。
Microorganisms in soil that decompose malodorous gas (10) include:
Nitrite bacteria that oxidize ammonia to nitrite, nitrate bacteria that oxidize nitrite to nitric acid, sulfide bacteria that decompose sulfides such as hydrogen sulfide, methyl mercaptabe, methyl sulfide, 1T acid, propionic acid, There are actinomycetes that decompose lower fatty acids such as butyric acid and valeric acid, and acidophilus and yeast that decompose tx'F acid, but the temperature at which these microorganisms can grow is approximately 5 -
60.0 and becomes dormant below about 5C.

しかし本発明では寒冷地でも悪臭ガス(10)の温度が
高温なので、土壌層(1)の温度を約5 C以下に低下
させることがない。
However, in the present invention, since the temperature of the malodorous gas (10) is high even in cold regions, the temperature of the soil layer (1) is not lowered below about 5C.

すなわち、寒冷地においても、土壌の温度を約6〜18
0に維持せしめ、土壌中の細菌などの微生物の分解力が
弱まることなく脱臭することが可能となっている。
In other words, even in cold regions, the soil temperature should be kept at about 6-18
This makes it possible to deodorize without weakening the decomposition power of microorganisms such as bacteria in the soil.

次に1実験例を説明する。Next, one experimental example will be explained.

堆肥化処理プラントt・ら発生する悪臭ガス中の主要な
悪臭物質とその濃度は次のとおりのものであった。
The main malodorous substances and their concentrations in the malodorous gas generated from the composting plant were as follows.

アンモニア4o ppm(以下同じ)、トリメチルアミ
ン0,1、硫化水素0.01.メチルメルカプタン0.
004. 硫化メチル0.04.二硫化メチル0.00
5.アセトアシデヒドa、9s、朴酸L43、プロピオ
ン酸0.0946、イン酪酸Q、Q636、n酪酸0.
0B’y4、イソ吉草酸0.0856、n吉草酸0.Q
O68、イソカブay酸0.05B、インブチルアルデ
ヒド0.150%罫酸メチルz1.3.軒酸エチ+b5
.63゜エタノール178 、nプロパツール 1.3
B、メチルエチルケトン1.55、αピネン0.39.
 βピネン0.0B、リモネン8.4Q、インペンタン
0.046、トシエンO+081 このような悪臭ガス(lO)を、 玉石層(3)の厚さ500m、m。
Ammonia 40 ppm (same below), trimethylamine 0.1, hydrogen sulfide 0.01. Methyl mercaptan 0.
004. Methyl sulfide 0.04. Methyl disulfide 0.00
5. Acetoacidehyde a, 9s, pactic acid L43, propionic acid 0.0946, inbutyric acid Q, Q636, n butyric acid 0.
0B'y4, isovaleric acid 0.0856, nvaleric acid 0. Q
O68, isocabayaic acid 0.05B, inbutyraldehyde 0.150% methyl sinter z1.3. Echi Echi + b5
.. 63゜Ethanol 178, nproper tool 1.3
B, methyl ethyl ketone 1.55, α-pinene 0.39.
β-pinene 0.0B, limonene 8.4Q, impentane 0.046, tosien O+081 Such foul-smelling gases (lO) were collected at a thickness of 500 m, m from the cobblestone layer (3).

砂利層(2)の厚さ200m、m。Gravel layer (2) thickness 200m, m.

土壌層(1)の厚さ600m、m。Thickness of soil layer (1) 600 m, m.

という条件で運転した時、従来の吸引ブロワを保温室内
に設置しない場合と本発明装置による場合との寒冷地に
おける運転結果は表1・のとおりである。
When operated under these conditions, Table 1 shows the operating results in a cold region when the conventional suction blower was not installed in the insulating room and when the device of the present invention was used.

表り 往、1.アンモニアの定量限界値はl ppm2、臭気
濃度は三点比較式臭袋法によって測定これによると従来
の方式では、外気の温度−100の場合、ブロワの運転
によって悪臭ガスの温度は少し4眉温し、脱臭装置入口
のダクト内では100であり、土壌層の深部ではO′″
C1浅部では−20と低下している。その結果アンモニ
ア濃度40ppmの悪臭ガスは20ppmにしか脱臭処
理されず、臭気濃度は4000より2000にしか脱臭
処理されなかった。
Appearance, 1. The quantitative limit value for ammonia is 1 ppm2, and the odor concentration is measured by the three-point comparison odor bag method.According to this, in the conventional method, when the outside air temperature is -100, the temperature of the malodorous gas is slightly reduced by 4 eyebrows when the blower is operated. However, it is 100 in the duct at the entrance of the deodorizing equipment, and O''' in the deep soil layer.
In the shallow part of C1, it decreases to -20. As a result, a malodorous gas with an ammonia concentration of 40 ppm was deodorized to only 20 ppm, and the odor concentration was reduced from 4000 to 2000.

とれは、東京都公害防止条令でf1種区域(居住専用地
域等)の排出口に規制さねている臭気濃度300に対し
て到底満足し得る数値ではない。
This is not a value that can be completely satisfied with the odor concentration of 300, which is not regulated by the Tokyo Metropolitan Pollution Prevention Ordinance for exhaust outlets in Class F1 areas (residential areas, etc.).

これ1(対し本発明の方式では、外気温度が−180と
低かった場合でも、脱臭装置入口のダクト内では3o”
cであり土壌層の深部の温度は12”o、浅部でも8 
Cと極端に低下することがなく、アンモニア濃度不検出
となって、臭気虚度3500の悪臭ガスは150とその
効果を説明する。
This 1 (on the other hand, with the method of the present invention, even if the outside air temperature is as low as -180 degrees, the inside of the duct at the entrance of the deodorizing equipment is 3 o"
c, and the temperature in the deep part of the soil layer is 12" o, and even in the shallow part it is 8" o.
C, the ammonia concentration is not detected, and the malodorous gas with an odor vacancy value of 3500 is 150.The effect will be explained below.

本発明は悪臭ガスの吸引ブロワの吸引運転自体で加熱さ
れた悪臭ガスの熱を逃がさないように同プロワを保温材
で形成する保温室に収容し、かつダクト配管も保温材で
保温して、この加熱保温された悪臭ガスを、玉石層、砂
利層を経て土壌層に放出するので、とぐに悪臭ガスの加
熱装置といったものが不必要となってその施設費および
維持運営費とも軽減されて経済的であるとともに、悪臭
ガスの脱臭効果は極めてよく厳格な都市条令の規制にも
満足し得る効果を挙げることができる。
In order to prevent the heat of the malodorous gas heated by the suction operation of the malodorous gas suction blower from escaping, the present invention houses the malodorous gas suction blower in an insulating chamber made of a heat insulating material, and also insulates the duct piping with a heat insulating material. This heated and heat-retained malodorous gas is released into the soil layer through the cobblestone layer and gravel layer, which immediately eliminates the need for a malodorous gas heating device, reducing facility costs and maintenance and operation costs. In addition, the deodorizing effect of malodorous gas is extremely good, and the effect can satisfy even strict city ordinances.

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

第1図は本装置の平面図、第2図は第1図のA −A線
縦断側面図である。 l・・・・土壌層 2・・・・砂利層 3・・・・玉石
層 5・・・排出孔 6・・・・ガス導管 7・・・・
吸引ブロワ 10・・・・悪臭ガス 12,12’・・
・・保温材 13・・・・保温室 14・・・・ダクト
配管 特許出願人株式会社 日 木製鋼所
FIG. 1 is a plan view of the present device, and FIG. 2 is a longitudinal sectional side view taken along the line A--A in FIG. 1. l... Soil layer 2... Gravel layer 3... Cobblestone layer 5... Discharge hole 6... Gas pipe 7...
Suction blower 10... Malodorous gas 12,12'...
・・Heat insulation material 13・・・・Insulation room 14・・Duct piping patent applicant Co., Ltd. Japan Wooden Steel Works

Claims (1)

【特許請求の範囲】[Claims] 保温材をもって形成した保温室内に吸引ブロワを設置し
、吸引プロワには、同ブロワの吸引運転により発生した
熱で加熱された悪臭ガスを導出するダクト配管を連設し
、ダクト配管は保温材をもって保温中るとともに、これ
に、多数の排出孔を有するガス導管を接続し、ガス導管
は玉石層中に埋設するととも尾、同層の上には砂利層を
、さらにその上には土壌層を積層した悪臭ガスの土壌に
よる脱臭装置。
A suction blower is installed in an insulating chamber made of heat insulating material, and a duct piping is connected to the suction blower to draw out the malodorous gas heated by the heat generated by the suction operation of the blower. At the same time as keeping it warm, a gas pipe with many discharge holes is connected to this, and the gas pipe is buried in a cobblestone layer.A gravel layer is placed on top of the cobblestone layer, and a soil layer is placed on top of that. A deodorizing device that uses soil to remove foul-smelling gas.
JP58115627A 1983-06-27 1983-06-27 Apparatus for deodorizing odorous gas by soil Pending JPS607923A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58115627A JPS607923A (en) 1983-06-27 1983-06-27 Apparatus for deodorizing odorous gas by soil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58115627A JPS607923A (en) 1983-06-27 1983-06-27 Apparatus for deodorizing odorous gas by soil

Publications (1)

Publication Number Publication Date
JPS607923A true JPS607923A (en) 1985-01-16

Family

ID=14667326

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58115627A Pending JPS607923A (en) 1983-06-27 1983-06-27 Apparatus for deodorizing odorous gas by soil

Country Status (1)

Country Link
JP (1) JPS607923A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6477790A (en) * 1987-07-02 1989-03-23 Ahlstroem Oy Pump delivery method and device for high-concentration pulp
JPH01159494A (en) * 1987-07-06 1989-06-22 A Ahlstroem Oy Method of separating gas from fluid force-fed by pump and pump for executing said method
JPH04263689A (en) * 1990-09-25 1992-09-18 A Ahlstroem Oy Method and device for discharging gas from liquid-solid mixture
JPH05508890A (en) * 1990-08-14 1993-12-09 エイ.アフルストロム コーポレーション Method and apparatus for improving the processing of gas-containing fiber suspensions

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5426512A (en) * 1977-08-01 1979-02-28 Eikou Sangiyou Kk Centrifugal blower
JPS5426511A (en) * 1977-07-29 1979-02-28 Kohkoku Chem Ind Air injection tube and air injection apparatus equipped therewith

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5426511A (en) * 1977-07-29 1979-02-28 Kohkoku Chem Ind Air injection tube and air injection apparatus equipped therewith
JPS5426512A (en) * 1977-08-01 1979-02-28 Eikou Sangiyou Kk Centrifugal blower

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6477790A (en) * 1987-07-02 1989-03-23 Ahlstroem Oy Pump delivery method and device for high-concentration pulp
JPH01159494A (en) * 1987-07-06 1989-06-22 A Ahlstroem Oy Method of separating gas from fluid force-fed by pump and pump for executing said method
JPH05508890A (en) * 1990-08-14 1993-12-09 エイ.アフルストロム コーポレーション Method and apparatus for improving the processing of gas-containing fiber suspensions
JPH04263689A (en) * 1990-09-25 1992-09-18 A Ahlstroem Oy Method and device for discharging gas from liquid-solid mixture

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