CN104707363B - Equipment for mechanically separating oil and pitch from gas condensate - Google Patents
Equipment for mechanically separating oil and pitch from gas condensate Download PDFInfo
- Publication number
- CN104707363B CN104707363B CN201410636765.4A CN201410636765A CN104707363B CN 104707363 B CN104707363 B CN 104707363B CN 201410636765 A CN201410636765 A CN 201410636765A CN 104707363 B CN104707363 B CN 104707363B
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- CN
- China
- Prior art keywords
- oil
- separator
- chamber
- tank
- condensate
- 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.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/001—Purifying combustible gases containing carbon monoxide working-up the condensates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0012—Settling tanks making use of filters, e.g. by floating layers of particulate material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0039—Settling tanks provided with contact surfaces, e.g. baffles, particles
- B01D21/0045—Plurality of essentially parallel plates
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/04—Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials
- C10K1/046—Reducing the tar content
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
Abstract
The present invention relates to the equipment for mechanically separating oil and pitch from gas condensate.Provide a kind of equipment for mechanically separating oil and pitch from gas condensate, it includes tank, the tank is equipped with the container that will be crossed by gas condensate, the container includes smelter coke, and the tank is equipped with parallel plate separators, wherein, vessel volume is divided into multiple rooms by separator, and oil and pitch are precipitated from gas condensate under the influence of gravity in the chamber.
Description
Technical field
The present invention relates to a kind of equipment for being mechanically decoupled oil and pitch from gas condensate, which includes tank,
The tank is equipped with the container that will be crossed by gas condensate, which includes coalescence ancillary equipment, and the tank is equipped with parallel-plate
Separator, wherein vessel volume is separated into multiple rooms by separator, and oily (oil) and pitch (tar) are in gravity in multiple room
Under the influence of from gas condensate precipitate.
Background technique
By means of fixed bed pressure gasification reactor, at high temperature and in most cases under superpressure, with steam
It,, should to obtain synthetic gas by solid fuel such as coal, coke or other carbonaceous fuel gasifyings with oxygen as gasifying medium
Synthetic gas includes carbon monoxide and hydrogen, wherein solid-state ash is obtained, which is discharged via ash discharge furnace from reactor,
The ash discharge furnace is formed rotary furnace in many cases.The reactor of the type is also frequently referred to as FBDB, and (=fixed bed is dry
Bottom) pressure gasifier.In the cooling period of output gas, gas condensate is formed.Here it is the gas from raw material (
In the case where coal) the condensed steam content of water content, undecomposed steam and form water, which passes through during gasification
The partial oxidation of hydrogen and obtain, which includes in the feed, referring to fourth edition Ullmannsder
Technischen Chemie, volume 14, page 449.
In biological purification plant before can be using gas condensate as wastewater treatment, for environmental protection and it can be used
The reason of recycling of product, gas condensate must be reprocessed.Firstly, oil, pitch and dust and subsequent phenol and ammonia quilt
It is separated from gas condensate.Therefore, in the incipient stage of these processing steps, oil and pitch by from gas condensate with machine
Tool mode is separated.
For being settling tank by oil and the equipment that is mechanically decoupled from gas condensate of pitch, in the settling tank, only by
In its density variation and gravity influence and impurity is separated from gas condensate.Equipment of the type itself is known
, referring to fourth edition UllmannsDer technischen Chemie, volume 14, page 450, Figure 59.
Therefore rougher pitch particle and oil droplet can be separated with reasonable measure from gas condensate.However, above-mentioned heavy
Shallow lake tank is not highly suited for separating lesser pitch particle and oil droplet, this is because separation process so carry out very slowly and
Need gas condensate be detained in these settling tanks for a long time and thus need the very big volume of these equipment and a large amount of
Space and cost.
Therefore, the purpose of the present invention is to provide a kind of equipment, using the equipment mechanically and with the sky of fair amount
Between and cost finer pitch and elaioleucite can also be separated from gas condensate.
Summary of the invention
The purpose is solved by equipment of the invention.
In order to separate, the present invention also utilizes the density variation between impurity, oil (oil) and pitch (tar) and water condensate.
For the coalescence for accelerating the oil droplet being emulsified in gas condensate and pitch to drip, first pass through gas condensate
Smelter coke filler, and then across parallel plate separators.The plate of these separators can also be formed corrugated plating, and
These separators are referred to as corrugated plating separator in this case.
Equipment according to the present invention is made of the outer tank with rectangular cross section.Tank can be opened or be closed towards atmosphere.
When carrying out the obtained ingredient of degasification to gas condensate and being discharged in a manner of environmental compatible, with closing form and 30 to
Design tank under the slight excess of 60mbar, 30 to the 60mbar slight excess for example, by be made of nitrogen air-flow superposition and
At.Air-flow is exited into from tank in cleaning device or for for example being burnt by means of blowpipe.
Outer tank is divided into multiple rooms by separator, and gas condensate crosses multiple room one by one.Inlet chamber is occupied
It is arranged in the middle part of tank middlely, and includes the filler with smelter coke.Filler is accommodated in rectangular vessel, which holds
The upper side and lower side of device is perforation, and filler is crossed by gas condensate.It, will via supplying duct below filler
Gas condensate to be cleaned is supplied in equipment.The bottom of room has opening with conical design and at deepest point,
The pitch discharge that the opening is used to sink in bottom.Second Room, that is, so-called oil separation chamber is located at the top of inlet chamber, gas
Body condensate is entered after crossing smelter coke in the oil separation chamber.
In the oil separation chamber, gas condensate logistics is split, so that each equal overflow is flowed in part passes through parallel-plate point
It is entered from device or corrugated plating separator in corresponding further last tank room, the parallel plate separators or corrugated plating point
From the left and right that device is arranged to inlet chamber.The shape in coke packing and in parallel plate separators or corrugated plating separator
At oil droplet rise in gas condensate at this and form oil reservoir on the surface.It will be from the oil reservoir via overflow weir
Oil takes out from tank.
Include in gas condensate pitch drop similarly coalesced in parallel plate separators or corrugated plating separator, and
And sink in the conical lower section of adjacent room of so-called condensate downstream chamber, separator leads to the cone of the adjacent room
Bottom.Then, pitch can be taken out from the conical lower section.
For separator between oil separation chamber and condensate downstream chamber equipped with channel, which immediately arrives the right side
Side and left, the channel are used to flow out simultaneously on the flow direction of gas condensate from parallel plate separators or corrugated plating separator
And the part oil risen at separator.
At advantageous aspect of the invention, conduit is connected to channel, and the conduit is excellent below liquid level in oil separation chamber
It selects and is slightly opened at 0.2m.By means of these conduits, avoid oil droplet partly taken away again by gas condensate logistics and cannot
Rise to surface.
Clean gas condensate is extracted from condensate downstream chamber via an overflow weir respectively.The overflow weir of oil separation chamber
Height and the height of overflow weir of condensate downstream chamber must adjust each other so that being extracted via the overflow weir of oil separation chamber big
Partial anhydrous oily phase.
The invention further relates to the purposes of equipment according to the present invention, for oil and pitch is mechanical from gas condensate
It separates, which obtains during the fixed bed pressure gasification of carbon-containing fuel, thus to obtain particularly advantageous point likes
From characteristic.
In short, the present invention provides a kind of equipment for mechanically separating oil and pitch from gas condensate, institute
Stating equipment includes the outer tank with rectangular cross section, and the outer tank is opened towards atmosphere and crossed by the gas condensate,
The equipment includes:
The first vertical separator of the first vertical separator of plane, the plane forms inlet chamber, the entrance
Room is for accommodating coalescent tank；First cone-shaped chamber bottom, first cone-shaped chamber bottom have bottom at its deepest point
Outlet, the outlet at bottom is for being discharged the pitch to avale；
Supplying duct, the supplying duct is for gas condensate to be cleaned to be introduced into described in the equipment
In mouth room；
Coalescent tank, the coalescent tank be with smelter coke fill rectangular vessel, the coalescent tank it is described enter
It is disposed in the top in the aperture of supplying duct in mouth room, the entire width of the outer tank is crossed transverse to the long side of the outer tank
Degree, the wall of the coalescent tank are perforation on the upper side and lower side, gas condensate are crossed from bottom described poly-
It ties agent tank and reaches top；
Parallel plate separators or corrugated plating separator, the parallel plate separators or corrugated plating separator are respectively arranged to institute
The left and right of inlet chamber is stated, the parallel plate separators or corrugated plating separator have the entire width for occupying the outer tank
Rectangular box form, wherein the parallel plate separators with respect to the horizontal plane at about 45 ° angle arrange；
The oil separation chamber of outer tank, upside and the parallel plate separators and vertical plane by the coalescent tank
The second separator, the oil separation chamber and remaining outer tank are spatially separating out, the second separator of the vertical plane
Abut directly against the lower outlet side of the parallel plate separators, wherein the oil separation chamber is opened upwardly toward atmosphere, wherein
Installation has the first overflow weir of discharge conduit, first overflow weir with discharge conduit in the top of the oil separation chamber
The liquid level being limited in the oil separation chamber, and via first overflow weir with discharge conduit by isolate oil from
The equipment discharge；
Condensate downstream chamber, the condensate downstream chamber is arranged to the left and right of the inlet chamber, by described
Second separator and the parallel plate separators separate the condensate downstream chamber with the oil separation chamber, and pass through institute
The first separator is stated to separate the condensate downstream chamber and the inlet chamber, wherein the parallel plate separators it is lower go out
The condensate downstream chamber is led in mouth side；
Wherein, second separator each be equipped with oil collection plate, wherein the long side of the oil collection plate each
The entire width for crossing the outer tank is horizontally extended, and the short side of the oil collection plate tilts down at a certain angle, so that
The oil risen at second separator from the parallel plate separators is collected below the oil collection plate, and in institute
State the lower section that one or more openings in the second separator are located at the oil collection plate, the oily energy accumulated below the oil collection plate
Enough entered in the oil separation chamber by one or more of openings；
Second cone-shaped chamber bottom, second cone-shaped chamber bottom have at its deepest point for going out for pitch to be discharged
Mouthful；Second overflow weir, second overflow weir are installed in the upper area of the condensate downstream chamber with discharge conduit
In, second overflow weir be used for the liquid level that is limited in the condensate downstream chamber and for by clean condensate water from
Oil and pitch discharge.
Preferably, conduit in addition is coupled in the opening in second separator, oil can by it is described in addition
Conduit overflow to top.
Preferably, the aperture of the other conduit is located at 0.2 meter of the lower section of the height of first overflow weir.
Preferably, the outer tank is closed relative to atmosphere, and the outer tank is equipped with entry conductor and delivery channel,
The entry conductor and the delivery channel are for introducing and being discharged air-flow, for the air-flow under the superpressure relative to atmosphere
It is superimposed the outer tank.
Preferably, the superpressure is the superpressure relative to atmosphere between 30 millibars and 60 millibars.
The invention further relates to the purposes according to equipment as described above, for oil and pitch is mechanical from gas condensate
Ground separation, the gas condensate obtain during the fixed bed pressure gasification of carbon-containing fuel.
Detailed description of the invention
It can also be obtained from the description of non-restrictive illustrative embodiment and label example and attached drawing of the invention into one
Exploitation, advantage and the possible application of step.Feature be described and/or diagram forms invention itself or with any combination side
Formula forms invention.
With reference to attached drawing, Fig. 1 and Fig. 2 will now describe equipment according to the present invention.
Fig. 1 shows the longitdinal cross-section diagram of equipment 1.
Fig. 2 shows the top view of equipment 1 (as passed through seen in cover).
Specific embodiment
Attached drawing is shown:
Equipment 1, the equipment 1 include outer tank 2 and the interior fittings being contained therein, which has rectangular cross section, should
Next equipment 1 will be described in detail；
Separator 3a, 3b, the separator 3a, 3b form inlet chamber 3, via supplying duct 5 by gas condensate to be cleaned
Object is supplied in the inlet chamber 3；
Coalescent tank 4 fills the coalescent tank 4 with smelter coke, and the upside 4b and downside 4a of the coalescent tank 4 are
It is perforation；
Parallel plate separators or corrugated plating separator 6a, 6b；
Separator 7a, 7b, separator 7a, 7b will be separated between oil separation chamber 7 and remaining ullage；
Oil collection plate 9a, 9b, oil collection plate 9a, 9b are mounted on separator 7a, 7b with a long side；
Conduit 10a, 10b, the conduit 10a, 10b guide the oil being collected into below oil collection plate, and the conduit 10a, 10b are passed through
It is reached below the summary of the liquid level 13 in oil separation chamber 7 in the opening not shown in the figure in corresponding separator；
Overflow weir 8 and adjacent discharge conduit, by the oil isolated from gas condensate from equipment 1 and from oil separation chamber 7
Pass through the overflow weir 8 and adjacent discharge conduit discharge；
Overflow weir 12a and 12b, overflow weir 12a and 12b have their discharge conduit being connected, will in the device
From oil and the clean gas condensate of pitch from equipment and from condensate downstream chamber 11a and 11b via overflow weir 12a and 12b
Discharge；
Conical lower section 3c, 11c and 11d, the conical lower section 3c, 11c and 11d have they at their deepest points
Discharge conduit, for pitch to be discharged.
Using the design of the equipment 1 relative to atmospheric exposure, superposition gas, such as nitrogen can be via 14 quilts of entry conductor
It is introduced into equipment and is discharged via delivery channel 15 from equipment.
Reference signs list
1 equipment according to the present invention
2 outer tanks
3 inlet chamber
3a, b separator
3c has the conical lower section of discharge conduit
4 coalescent tanks
The pot bottom of 4a, b perforation
5 supplying ducts
6a, b parallel plate separators or corrugated plating separator
7 oil separation chambers
7a, b separator
8 have the overflow weir of discharge conduit
9a, b oil collection plate
10a, b conduit
11a, b condensate downstream chamber
11c, d have the conical lower section of discharge conduit
12a, b have the overflow weir of discharge conduit
13 liquid levels
14 for being superimposed the entry conductor of gas
15 for being superimposed the delivery channel of gas
Claims (6)
1. a kind of equipment (1) for mechanically separating oil and pitch from gas condensate, the equipment (1) includes having
The outer tank (2) of rectangular cross section, the outer tank (2) are opened and are crossed by the gas condensate, the equipment towards atmosphere
(1) include:
Vertical the first separator (3a, 3b) of vertical the first separator (3a, 3b) of plane, the plane forms inlet chamber
(3), the inlet chamber (3) is for accommodating coalescent tank (4)；First cone-shaped chamber bottom (3c), first cone-shaped chamber bottom
Portion (3c) has outlet at bottom at its deepest point, and the outlet at bottom is for being discharged the pitch to avale；
Supplying duct (5), the supplying duct (5) are used to gas condensate to be cleaned being introduced into the equipment (1)
In the inlet chamber (3)；
Coalescent tank (4), the coalescent tank (4) are the rectangular vessels filled with smelter coke, and the coalescent tank (4) is in institute
The top for being disposed in the aperture of supplying duct (5) in inlet chamber (3) is stated, crosses institute transverse to the long side of the outer tank (2)
The entire width of outer tank (2) is stated, the wall of the coalescent tank (4) is perforation on upside (4b) and downside (4a), makes to bring about the desired sensation
Body condensate can cross the coalescent tank (4) from bottom and reach top；
Parallel plate separators or corrugated plating separator, the parallel plate separators or corrugated plating separator enter described in being respectively arranged to
The left and right of mouth room (3), the parallel plate separators or corrugated plating separator have the entire width for occupying the outer tank (2)
The form of the rectangular box of degree, wherein the parallel plate separators are arranged with the angle with respect to the horizontal plane at about 45 °；
The oil separation chamber (7) of outer tank (2), by the upside (4b) of the coalescent tank and the parallel plate separators and vertically
Plane the second separator (7a, 7b), the oil separation chamber (7) is spatially separating out with remaining outer tank, it is described vertical
The second separator (7a, 7b) of plane abuts directly against the lower outlet side of the parallel plate separators, wherein the oil separation chamber
(7) it is opened upwardly toward atmosphere, wherein installation has the first overflow of discharge conduit in the top of the oil separation chamber (7)
Weir (8), first overflow weir (8) with discharge conduit are limited to the liquid level in the oil separation chamber (7), and via institute
It states the first overflow weir (8) with discharge conduit the oil isolated is discharged from the equipment (1)；
Condensate downstream chamber (11a, 11b), the condensate downstream chamber (11a, 11b) are arranged to a left side for the inlet chamber (3)
Side and right, by second separator (7a, 7b) and the parallel plate separators by the condensate downstream chamber (11a,
It 11b) is separated with the oil separation chamber (7), and passes through first separator (3a, 3b) for the condensate downstream chamber
(11a, 11b) is separated with the inlet chamber (3), wherein the lower outlet side of the parallel plate separators leads to the condensate
Downstream chamber (11a, 11b)；
Wherein, second separator (7a, 7b) each be equipped with oil collection plate (9a, 9b), wherein the length of the oil collection plate
Each horizontally extends the entire width for crossing the outer tank (2) on side, and the short side of the oil collection plate is at a certain angle
It tilts down, so that the oil risen at second separator (7a, 7b) from the parallel plate separators is in the oil collection plate
It is collected below (9a, 9b), and one or more openings in second separator (7a, 7b) are located at the oil-collecting
The lower section of plate, the oil accumulated below the oil collection plate can enter the oil separation chamber by one or more of openings
(7) in；
Second cone-shaped chamber bottom (11c, 11d), second cone-shaped chamber bottom (11c, 11d) has at its deepest point to be used
In the outlet of discharge pitch；Second overflow weir (12a, 12b), second overflow weir (12a, 12b) are installed in discharge
In the upper area of the condensate downstream chamber (11a, 11b) of conduit, second overflow weir (12a, 12b) is for being limited to
Liquid level in the condensate downstream chamber (11a, 11b) and for clean condensate water to be discharged from oil and pitch.
2. equipment according to claim 1, it is characterised in that: conduit (10a, 10b) in addition is coupled in described
Opening in two compartment part (7a, 7b), oil can overflow to top by the other conduit (10a, 10b).
3. equipment according to claim 2, it is characterised in that: the aperture of the other conduit is located at first overflow
At 0.2 meter of the lower section of the height on weir (8).
4. equipment according to any one of claims 1 to 3, it is characterised in that: the outer tank (2) is relative to atmosphere
It is closed, and the outer tank (2) be equipped with entry conductor (14) and delivery channel (15), the entry conductor (14) and it is described out
Mouth conduit (15) is for introducing and being discharged air-flow, for being superimposed the outer tank (2) with the air-flow under the superpressure relative to atmosphere.
5. equipment according to claim 4, it is characterised in that: the superpressure is relative to atmosphere in 30 millibars and 60 millibars
Between superpressure.
6. the purposes of equipment according to any one of claims 1 to 5, for by oil and pitch from gas condensate machine
It separates to tool formula, the gas condensate obtains during the fixed bed pressure gasification of carbon-containing fuel.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102013114116.1 | 2013-12-16 | ||
| DE102013114116.1A DE102013114116B4 (en) | 2013-12-16 | 2013-12-16 | Device for the mechanical separation of oil and tar from gas condensate and use of the device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104707363A CN104707363A (en) | 2015-06-17 |
| CN104707363B true CN104707363B (en) | 2019-04-26 |
Family
ID=52003791
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420678770.7U Withdrawn - After Issue CN204582612U (en) | 2013-12-16 | 2014-11-06 | For the equipment that oil and pitch are mechanically separated from gas condensate |
| CN201410636765.4A Active CN104707363B (en) | 2013-12-16 | 2014-11-06 | Equipment for mechanically separating oil and pitch from gas condensate |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420678770.7U Withdrawn - After Issue CN204582612U (en) | 2013-12-16 | 2014-11-06 | For the equipment that oil and pitch are mechanically separated from gas condensate |
Country Status (4)
| Country | Link |
|---|---|
| CN (2) | CN204582612U (en) |
| AU (1) | AU2014365396B2 (en) |
| DE (1) | DE102013114116B4 (en) |
| WO (1) | WO2015090981A1 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102013114116B4 (en) * | 2013-12-16 | 2016-06-09 | L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude | Device for the mechanical separation of oil and tar from gas condensate and use of the device |
| CN107297088A (en) * | 2016-04-14 | 2017-10-27 | 黑珀（上海）工业技术有限公司 | A kind of conduction oil cleaning treatment system |
| CN107585731A (en) * | 2017-09-29 | 2018-01-16 | 江苏云端重工科技有限公司 | A kind of Bituminous concrete surface reclaims charging aperture |
| KR102614264B1 (en) * | 2019-09-19 | 2023-12-18 | 주식회사 엘지화학 | Neutralization/Water Separate Tank For Esterification Products And The Method For Neutralizing/Water Separating Esterification Products |
| CN112591325B (en) * | 2020-11-27 | 2022-07-26 | 安徽工业大学 | Mechanical slag discharge type conical bottom type tar storage tank |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN204582612U (en) * | 2013-12-16 | 2015-08-26 | 乔治·克劳德方法的研究开发空气股份有限公司 | For the equipment that oil and pitch are mechanically separated from gas condensate |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1309930A (en) * | 1969-07-07 | 1973-03-14 | Pielkenrood Vinitex Bv | Separators for removing flotation and or precipitation components from a liquid |
| DE2543532C3 (en) * | 1975-09-30 | 1980-10-30 | Metallgesellschaft Ag, 6000 Frankfurt | Process for the gravity separation of an aqueous tar-containing condensate |
| DE2607745C2 (en) * | 1976-02-26 | 1984-03-15 | Metallgesellschaft Ag, 6000 Frankfurt | Process for treating condensate from the cooling of raw gas from the pressurized gasification of solid fuels |
| DD156166B1 (en) * | 1981-02-05 | 1986-06-25 | Reiner Kinder | METHOD FOR CONTAINING CONDENSES AND WAITERS |
| DE59813936D1 (en) * | 1998-04-29 | 2007-04-19 | Sulzer Chemtech Ag | A method of separating a first from a second liquid |
| CN2477617Y (en) * | 2000-10-27 | 2002-02-20 | 胜利石油管理局勘察设计研究院 | Pressure oil removing settling pot |
| CN201333333Y (en) * | 2008-12-24 | 2009-10-28 | 江苏艾特克实业有限公司 | Novel oil-water separator |
| CN201643790U (en) * | 2010-04-15 | 2010-11-24 | 中国石油化工股份有限公司 | Oil-water separator |
| IT1404151B1 (en) * | 2010-12-29 | 2013-11-15 | Eni Spa | SEPARATION APPARATUS BY COALESCENCE OF A MIXTURE INCLUDING TWO FLUID PHASES BETWEEN THEM IMMERSIBLE AND DIFFERENT SPECIFIC DENSITY |
| CN202289570U (en) * | 2011-10-24 | 2012-07-04 | 北京百恒达石油技术有限公司 | Efficient oil-gas-water separator |
-
2013
- 2013-12-16 DE DE102013114116.1A patent/DE102013114116B4/en active Active
-
2014
- 2014-11-06 CN CN201420678770.7U patent/CN204582612U/en not_active Withdrawn - After Issue
- 2014-11-06 CN CN201410636765.4A patent/CN104707363B/en active Active
- 2014-12-04 AU AU2014365396A patent/AU2014365396B2/en active Active
- 2014-12-04 WO PCT/EP2014/076489 patent/WO2015090981A1/en active Application Filing
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN204582612U (en) * | 2013-12-16 | 2015-08-26 | 乔治·克劳德方法的研究开发空气股份有限公司 | For the equipment that oil and pitch are mechanically separated from gas condensate |
Also Published As
| Publication number | Publication date |
|---|---|
| AU2014365396B2 (en) | 2018-02-22 |
| CN204582612U (en) | 2015-08-26 |
| DE102013114116B4 (en) | 2016-06-09 |
| CN104707363A (en) | 2015-06-17 |
| WO2015090981A1 (en) | 2015-06-25 |
| AU2014365396A1 (en) | 2016-07-21 |
| DE102013114116A1 (en) | 2015-06-18 |
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