CN105238556A - Centrifuged oil residue separation and purification integration machine - Google Patents
Centrifuged oil residue separation and purification integration machine Download PDFInfo
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- CN105238556A CN105238556A CN201510597680.4A CN201510597680A CN105238556A CN 105238556 A CN105238556 A CN 105238556A CN 201510597680 A CN201510597680 A CN 201510597680A CN 105238556 A CN105238556 A CN 105238556A
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Abstract
A centrifuged oil residue separation and purification integration machine is characterized in that a dephosphorization circulating pump pumps external crude oil into a dephosphorization barrel through an oil conveying pipeline, water steam generated by using a steam production system is conveyed to the crude oil through a high pressure gas tube, and the water steam is mutually blended with oil residues in the dephosphorization barrel to make the specific gravity of the oil residues be larger than that of oil in order to realize a dephosphorization effect; an oil material in the dephosphorization barrel is sent into the inner cavity of a rotating drum through a second high pressure oil tube by an oil pump after dephosphorization is completed, the rotating drum and a screw propulsion shaft run at a high speed under the driving of a main motor, a solid phase with large mass tightly cling to the inner wall of the rotating drum, and relative movement of the rotating drum and the screw propulsion shaft makes a blade on the screw propulsion shaft discharge the solid phase clinging to the inner wall of the rotating drum to a residue discharge chamber; and clear oil obtained after separation flows to the large end of the rotating drum, and flows to an oil chamber from an oil outlet on a hollow shaft in order to realize oil-residue separation of the crude oil. The purpose of the invention is to provide the centrifuged oil residue separation and purification integration machine with the advantages of good dephosphorization effect, compact structure, good working continuity, high working efficiency, small manual labor intensity and good oil product quality.
Description
Technical field
The present invention relates to a kind of crude oil dregs of fat separating device.
Background technology
Crude oil refer generally to from leach or squeezing process by the grease of some impurity containing inedibility extracted vegetable oil material, the existence of hair well cuts can have a strong impact on carrying out smoothly of grease following process, affect the safe storage of grease, reduce quality and the use value of grease, the particularly existence of phosphatide in crude oil, grease turbid appearance, dimness can be made, a large amount of foam can be produced when cooking and produce black muddiness, therefore need to carry out refining to remove phosphatide to crude oil, also need to remove the solid phase in crude oil simultaneously.Existing dregs of fat separating device all can't do without the intermediate medium such as filter screen, filter cloth when processing crude oil, there is processing power low, can not work continuously, the defects such as labour intensity is large.
Summary of the invention
The object of the present invention is to provide that a kind of dephosphorization effect is good, compact construction, work continuity is good, working efficiency is high, hand labor intensity is little, the measured centrifugal dregs of fat of oil quality are separated refining all-in-one.
The centrifugal dregs of fat of the present invention are separated refining all-in-one, comprise frame, also comprise vapour system processed, dephosphorization system, centrifugal dregs of fat separation host.
Described vapour system processed comprises casing, described casing is provided with water intaking valve, described water intaking valve is connected with the vapor can being arranged on described casing internal by pipeline, in described vapor can, electric heating tube is installed, the end of electric heating tube is threaded connection and is fixed on the sidewall of vapor can, gap between described electric heating tube and vapor can inwall adopts gasket seal, lagging material is provided with between described vapor can and casing, described casing is provided with tensimeter and liquidometer, the top of described casing is provided with gas outlet valve, described tensimeter, liquidometer and gas outlet valve are connected to vapor can inside by pipeline.
Described dephosphorization system comprises dephosphorization recycle pump, dephosphorization bucket and transition pipeline, the crude oil of outside is evacuated in dephosphorization bucket by transition pipeline by described dephosphorization recycle pump, described gas outlet valve connects the bottom of dephosphorization bucket by the high-pressure air pipe being in series with vacuum breaker, dephosphorization bottom of the barrel is also provided with threeway, the entrance of described threeway is connected with described dephosphorization bucket, the left outlet of described threeway is connected with dephosphorization recycle pump by pipeline, and the right outlet of described threeway is connected with oil pump by the first high-pressure line.
Described centrifugal dregs of fat separation host comprises the tubular shaft arranged in left-right direction, described tubular shaft is arranged in frame by left shaft holder, the right-hand member of described tubular shaft is connected with the left end of rotary drum, the left side of described rotary drum is hollow cylinder, the right-hand part of described rotary drum is hollow round table, the cone angle of round platform is towards right-hand member, the right-hand member of described rotary drum is arranged on the right-hand member of spiral promoting shaft by cone end bearing box, the left end of spiral promoting shaft is arranged in tubular shaft by the second bearing, the middle part of spiral promoting shaft is positioned at rotary drum, the right-hand member of spiral promoting shaft is arranged on described frame right part by right bearing seat.
Be provided with grease chamber outside described tubular shaft, described tubular shaft is provided with the outlet-port of multiple connection grease chamber and described rotary drum internal cavity left end; Be provided with deslagging chamber outside described rotary drum right-hand member, the right-hand member of described rotary drum is provided with the mud hole of multiple connection deslagging chamber.
Right-hand part in described spiral promoting shaft is provided with oil transportation material pipeline vertically, the left end of oil transportation material pipeline is provided with oil extraction material hole, oil extraction material hole is communicated with the middle part of rotary drum internal cavity, the right-hand member of oil transportation material pipeline communicates with the left outlet of L-type three-way valve, L-type three-way valve is arranged on described right bearing seat by terminal pad, gap between L-type three-way valve and right bearing seat adopts inlet nozzle oil sealing sealing, and described oil pump is communicated by the entrance of the second high-pressure line with L-type three-way valve; The right outlet of L-type three-way valve is connected with dephosphorization bucket;
The left end of described tubular shaft is provided with rotary drum synchronizing wheel, the shaft shoulder that the left end of described spiral promoting shaft stretches out tubular shaft is provided with spiral promoting shaft synchronizing wheel, rotary drum synchronizing wheel, spiral promoting shaft synchronizing wheel is respectively by rotary drum Timing Belt, spiral promoting shaft Timing Belt is connected with the duplex synchronizing wheel transmission on main motor output shaft, the number of teeth utilizing synchronizing wheel different and pitch operate to the differential realizing rotary drum and spiral promoting shaft, under the differential action of centrifugal force and rotary drum and spiral promoting shaft, in oil plant, solid phase pushes mud hole to by the screw-blade on spiral promoting shaft, and got rid of in deslagging chamber, edible vegetable oil is then flow in grease chamber by outlet-port.
Preferably, described vapor can cross section is oval or circular, and described bottom of shell is provided with 3-6 legs.
Preferably, be also provided with pilot lamp outside described casing, described gas outlet valve is electric check valve or hand stop valve.
Preferably, described casing is provided with rly., air switch, warning howler, controller and power switch.
Preferably, described dephosphorization bucket is fixed on rear side of described frame.
Preferably, described grease chamber is arranged on left shaft holder, and described deslagging chamber is arranged on described right bearing seat.
Preferably, also comprise power control system and primary source box, described primary source box is arranged on the middle front end bottom described frame, and described power control system, dephosphorization recycle pump, oil pump are all connected primary source box by electric wire with mair motor.
Preferably, the bottom of described frame is provided with 4-6 rubber shock-absorbing pin.
The centrifugal dregs of fat of the present invention are separated in refining all-in-one, the crude oil of outside is evacuated in dephosphorization bucket by transition pipeline by dephosphorization recycle pump, the water vapor that vapour system processed produces is transported in crude oil by high-pressure air pipe, water vapor merges mutually at dephosphorization bucket and the dregs of fat, dregs of fat proportion is become sink than oil, to reach the effect of dephosphorization; After dephosphorization completes, by oil pump, the oil plant in dephosphorization bucket is sent into rotary drum inner chamber through the second high-pressure line, under mair motor drives, rotary drum and spiral promoting shaft run up, enter the oil plant of rotary drum inner chamber under centrifugal action, the solid phase that quality is large can tightly be bonded on the inwall of rotary drum, under the effect of differential, relative movement between rotary drum and spiral promoting shaft makes the blade on spiral promoting shaft that the solid phase be bonded on drum inner wall is pushed to rotary drum cone end mud hole place, side, and gets rid of under the influence of centrifugal force to deslagging chamber; Edible vegetable oil after separation then flows to the large end of rotary drum by the helical channel between rotary drum and spiral promoting shaft, flows out to grease chamber by the outlet-port on tubular shaft, and the dregs of fat realizing crude oil are separated.Compact overall structure of the present invention; be separated the oil product obtained limpid pure bright; and owing to there is no filtration medium; so midway does not need to shut down troublesome operation such as changing filter cloth; keep on the one hand working continuously, do not need artificial frequent scarfing cinder on the other hand, dismounting, erecting equipment; reduce hand labor intensity, improve working efficiency.
Be separated refining all-in-one below in conjunction with accompanying drawing to the centrifugal dregs of fat of the present invention to be described further.
Accompanying drawing explanation
Fig. 1 is that the centrifugal dregs of fat of the present invention are separated refining all-in-one machine structure schematic diagram;
Fig. 2 is vapour system architecture schematic diagram processed in the present invention.
Embodiment
The centrifugal dregs of fat of the present invention are separated refining all-in-one, and the centrifugal dregs of fat are separated refining all-in-one, and comprise frame 17, the bottom of frame 17 is provided with 4,5 or 6 rubber shock-absorbing pin 20, also comprises vapour system processed, dephosphorization system, centrifugal dregs of fat separation host.
Vapour system processed comprises casing 1, casing is provided with water intaking valve, water intaking valve is connected with the vapor can 3 being arranged on casing 1 inside by pipeline, electric heating tube 4 is installed in vapor can 3, the end of electric heating tube 4 be threaded connection be fixed on vapor can 3 sidewall on, gap between electric heating tube 4 and vapor can 3 inwall adopts gasket seal, lagging material is provided with between vapor can 3 and casing 1, casing 1 is provided with tensimeter 5 and liquidometer, the top of casing 1 is provided with gas outlet valve 6, and it is inner that tensimeter 5, liquidometer and gas outlet valve 6 is connected to vapor can 3 by pipeline.Vapor can 3 cross section can be ellipse or circle, is provided with 3 or 4 or 5 or 6 legs 12 bottom casing 1.Also be provided with pilot lamp 7 outside casing 1, gas outlet valve 6 is electric check valve or hand stop valve, to control quantity of steam.Casing 1 is provided with rly. 8, air switch 9, warning howler 10, controller 11 and power switch 2.Air switch 9 controls the circuit of whole vapour system processed, and disconnect air switch 9, vapour system internal circuit processed quits work.Power switch 2 controls the electric heating tube 4 in vapor can 3.The water level in vapor can 3 monitored by controller 11, in case electric heating tube 4 dry combustion method causes damage.
Dephosphorization system comprises dephosphorization recycle pump 19, dephosphorization bucket 24 and transition pipeline, dephosphorization bucket 24 is fixed on rear side of frame 17, the crude oil of outside is evacuated in dephosphorization bucket 24 by transition pipeline by dephosphorization recycle pump 19, gas outlet valve 6 connects the bottom of dephosphorization bucket 24 by the high-pressure air pipe being in series with vacuum breaker, threeway 40 is also provided with bottom dephosphorization bucket 24, the entrance of threeway 40 is connected with dephosphorization bucket 24, the left outlet of threeway 40 is connected with dephosphorization recycle pump 19 by pipeline, and the right outlet of threeway 40 is connected with oil pump 18 by the first high-pressure line.
Centrifugal dregs of fat separation host comprises the tubular shaft 26 arranged in left-right direction, tubular shaft 26 is arranged in frame 17 by left shaft holder 27, the right-hand member of tubular shaft 26 is connected with the left end of rotary drum 25, the left side of rotary drum 25 is hollow cylinder, the right-hand part of rotary drum 25 is hollow round table, the cone angle of round platform is towards right-hand member, the right-hand member of rotary drum 25 is arranged on the right-hand member of spiral promoting shaft 22 by cone end bearing box 21, the left end of spiral promoting shaft 22 is arranged in tubular shaft 26 by the second bearing 32, the middle part of spiral promoting shaft 22 is positioned at rotary drum 25, the right-hand member of spiral promoting shaft 22 is arranged on frame 17 right part by right bearing seat 16.
Be provided with grease chamber 29 outside tubular shaft 26, and grease chamber 29 is arranged on left shaft holder 27, tubular shaft 26 is provided with the outlet-port 38 of multiple connection grease chamber 29 and rotary drum 25 internal cavity left end; Be provided with deslagging chamber 13 outside rotary drum 25 right-hand member, and deslagging chamber 13 is arranged on right bearing seat 16, the right-hand member of rotary drum 25 is provided with the mud hole 37 of multiple connection deslagging chamber 13.
Right-hand part in described spiral promoting shaft 22 is provided with oil transportation material pipeline 35 vertically, the left end of oil transportation material pipeline 35 is provided with oil extraction material hole 36, oil extraction material hole 36 is communicated with the middle part of rotary drum 25 internal cavity, the right-hand member of oil transportation material pipeline 35 communicates with the left outlet of L-type three-way valve 41, L-type three-way valve 41 is arranged on described right bearing seat 16 by terminal pad, gap between L-type three-way valve 41 and right bearing seat 16 adopts inlet nozzle oil sealing 15 to seal, and described oil pump 18 is communicated with the entrance of L-type three-way valve 41 by the second high-pressure line 34.The right outlet of L-type three-way valve 41 is connected with dephosphorization bucket 24, and oil pump 18 also plays effect dephosphorization bucket being carried out to circulation stirring, strengthens dephosphorization effect.
The left end of tubular shaft 26 is provided with rotary drum synchronizing wheel, the shaft shoulder that the left end of spiral promoting shaft 22 stretches out tubular shaft 26 is provided with spiral promoting shaft synchronizing wheel, rotary drum synchronizing wheel, spiral promoting shaft synchronizing wheel is respectively by rotary drum Timing Belt, spiral promoting shaft Timing Belt is connected with duplex synchronizing wheel 39 transmission on mair motor 30 output shaft, duplex synchronizing wheel 39 is combination synchronizing wheel, be combined into one by the synchronizing wheel of two different numbers of teeth and different pitch, the number of teeth utilizing synchronizing wheel different and pitch operate to realize rotary drum 25 with the differential of spiral promoting shaft 22, during work, the rotating speed of rotary drum 25 is a little more than the rotating speed of spiral promoting shaft 22, at centrifugal force and rotary drum 25 with under the differential action of spiral promoting shaft 22, in oil plant, solid phase pushes mud hole 37 to by the screw-blade on spiral promoting shaft 22, and got rid of in deslagging chamber 13, edible vegetable oil is then flow in grease chamber 29 by outlet-port 38.
The centrifugal dregs of fat of the present invention are separated refining all-in-one, also be provided with power control system 23 and primary source box 31, primary source box 31 is arranged on the middle front end bottom frame 17, and power control system 23, dephosphorization recycle pump 19, oil pump 18 are all connected primary source box 31 by electric wire with mair motor 30.
When the centrifugal dregs of fat of the present invention are separated the work of refining all-in-one, need to be cooled between 70 ~ 85 DEG C first by the crude oil of squeezing out, crude oil is in this temperature range, the dregs of fat that the centrifugal dregs of fat of the present invention are separated refining all-in-one are separated refining effect the best, then the crude oil cooled is evacuated in dephosphorization bucket 24 by transition pipeline by dephosphorization recycle pump 19, the water vapor that vapour system processed produces is transported in crude oil by high-pressure air pipe, water vapor merges mutually at dephosphorization bucket 24 and the dregs of fat, dregs of fat proportion is become sink than oil, to reach the effect of dephosphorization, after dephosphorization completes, by oil pump 18, the oil plant in dephosphorization bucket 24 is sent into rotary drum 25 inner chamber through the second high-pressure oil 34 pipe, under mair motor 30 drives, rotary drum 25 and spiral promoting shaft 22 run up, enter the oil plant of rotary drum 25 inner chamber under centrifugal action, the solid phase that quality is large can tightly be bonded on the inwall of rotary drum 25, under the effect of differential, relative movement between rotary drum 25 and spiral promoting shaft 22 makes the blade on spiral promoting shaft that the solid phase be bonded on rotary drum 25 inwall is pushed to rotary drum 25 to bore and hold side mud hole 37 place, and get rid of to deslagging chamber 13 under the influence of centrifugal force, edible vegetable oil after separation then flows to rotary drum 25 by the helical channel between rotary drum 25 and spiral promoting shaft 22 and holds greatly, flows out to grease chamber 29 by the outlet-port 38 on tubular shaft 26, and the dregs of fat realizing crude oil are separated.
The centrifugal dregs of fat of the present invention are separated refining all-in-one, utilize in mixed solution and have different densities and immiscible light liquid and solid phase, obtain the principle of different settling velocity in centrifuge field, reach the object of solid phase particles sedimentation in separating liquid.The present invention is mainly used in the separation that solid phase particle diameter is the liquid-solid two-phase suspension of 0.01-3mm, has the advantages such as the high and operating maintenance of continuous running, screw unloading, compact construction, separation efficiency is convenient.Be widely used in rural area oil expression, oil strain industry, also may be used for field and industry that food, environmental protection, chemical industry etc. need solid-liquid separation.
Claims (8)
1. the centrifugal dregs of fat are separated refining all-in-one, comprise frame (17), it is characterized in that: also comprise vapour system processed, dephosphorization system, centrifugal dregs of fat separation host;
Described vapour system processed comprises casing (1), described casing is provided with water intaking valve, described water intaking valve is connected by the vapor can (3) that pipeline is inner with being arranged on described casing (1), electric heating tube (4) is installed in described vapor can (3), the end of electric heating tube (4) be threaded connection be fixed on vapor can (3) sidewall on, gap between described electric heating tube (4) and vapor can (3) inwall adopts gasket seal, lagging material is provided with between described vapor can (3) and casing (1), described casing (1) is provided with tensimeter (5) and liquidometer, the top of described casing (1) is provided with gas outlet valve (6), described tensimeter (5), it is inner that liquidometer and gas outlet valve (6) are connected to vapor can (3) by pipeline,
Described dephosphorization system comprises dephosphorization recycle pump (19), dephosphorization bucket (24) and transition pipeline, the crude oil of outside is evacuated in dephosphorization bucket (24) by transition pipeline by described dephosphorization recycle pump (19), described gas outlet valve (6) connects the bottom of dephosphorization bucket (24) by the high-pressure air pipe being in series with vacuum breaker, dephosphorization bucket (24) bottom is also provided with threeway (40), the entrance of described threeway (40) is connected with described dephosphorization bucket (24), the left outlet of described threeway (40) is connected with dephosphorization recycle pump (19) by pipeline, the right outlet of described threeway (40) is connected with oil pump (18) by the first high-pressure line,
Described centrifugal dregs of fat separation host comprises the tubular shaft (26) arranged in left-right direction, described tubular shaft (26) is arranged in frame (17) by left shaft holder (27), the right-hand member of described tubular shaft (26) is connected with the left end of rotary drum (25), the left side of described rotary drum (25) is hollow cylinder, the right-hand part of described rotary drum (25) is hollow round table, the cone angle of round platform is towards right-hand member, the right-hand member of described rotary drum (25) is arranged on the right-hand member of spiral promoting shaft (22) by cone end bearing box (21), the left end of spiral promoting shaft (22) is arranged in tubular shaft (26) by the second bearing (32), the middle part of spiral promoting shaft (22) is positioned at rotary drum (25), the right-hand member of spiral promoting shaft (22) is arranged on described frame (17) right part by right bearing seat (16),
Be provided with grease chamber (29) outside described tubular shaft (26), described tubular shaft (26) is provided with the outlet-port (38) of multiple connection grease chamber (29) and described rotary drum (25) internal cavity left end; Be provided with deslagging chamber (13) outside described rotary drum (25) right-hand member, the right-hand member of described rotary drum (25) is provided with the mud hole (37) of multiple connection deslagging chamber (13);
Right-hand part in described spiral promoting shaft (22) is provided with oil transportation material pipeline (35) vertically, the left end of oil transportation material pipeline (35) is provided with oil extraction material hole (36), oil extraction material hole (36) is communicated with the middle part of rotary drum (25) internal cavity, the right-hand member of oil transportation material pipeline (35) communicates with the left outlet of L-type three-way valve (41), L-type three-way valve (41) is arranged on described right bearing seat (16) by terminal pad, gap between L-type three-way valve (41) and right bearing seat (16) adopts inlet nozzle oil sealing (15) to seal, described oil pump (18) is communicated by the entrance of the second high-pressure line (34) with L-type three-way valve (41), the right outlet of L-type three-way valve (41) is connected with dephosphorization bucket (24),
The left end of described tubular shaft (26) is provided with rotary drum synchronizing wheel, the shaft shoulder that the left end of described spiral promoting shaft (22) stretches out tubular shaft (26) is provided with spiral promoting shaft synchronizing wheel, rotary drum synchronizing wheel, spiral promoting shaft synchronizing wheel is respectively by rotary drum Timing Belt, spiral promoting shaft Timing Belt is connected with duplex synchronizing wheel (39) transmission on mair motor (30) output shaft, the number of teeth utilizing synchronizing wheel different and pitch operate to realize rotary drum (25) with the differential of spiral promoting shaft (22), under centrifugal force and rotary drum (25) differential action with spiral promoting shaft (22), in oil plant, solid phase pushes mud hole (37) to by the screw-blade on spiral promoting shaft (22), and got rid of in deslagging chamber (13), edible vegetable oil is then flow in grease chamber (29) by outlet-port (38).
2. the centrifugal dregs of fat according to claim 1 are separated refining all-in-one, it is characterized in that: described vapor can (3) cross section is for oval or circular, and described casing (1) bottom is provided with 3-6 legs (12).
3. the centrifugal dregs of fat according to claim 2 are separated refining all-in-one, it is characterized in that: described casing (1) outside is also provided with pilot lamp (7), and described gas outlet valve (6) is electric check valve or hand stop valve.
4. the centrifugal dregs of fat according to claim 3 are separated refining all-in-one, it is characterized in that: described casing (1) is provided with rly. (8), air switch (9), warning howler (10), controller (11) and power switch (2).
5. the centrifugal dregs of fat according to claim 4 are separated refining all-in-one, it is characterized in that: described dephosphorization bucket (24) is fixed on described frame (17) rear side.
6. the centrifugal dregs of fat according to claim 5 are separated refining all-in-one, and it is characterized in that: described grease chamber (29) are arranged on left shaft holder (27), described deslagging chamber (13) is arranged on described right bearing seat (16).
7. the centrifugal dregs of fat according to claim 6 are separated refining all-in-one, it is characterized in that: also comprise power control system (23) and primary source box (31), described primary source box (31) is arranged on the middle front end of described frame (17) bottom, and described power control system (23), dephosphorization recycle pump (19), oil pump (18) are all connected primary source box (31) by electric wire with mair motor (30).
8. the centrifugal dregs of fat according to claim 7 are separated refining all-in-one, it is characterized in that: the bottom of described frame (17) is provided with 4-6 rubber shock-absorbing pin (20).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510597680.4A CN105238556A (en) | 2015-09-20 | 2015-09-20 | Centrifuged oil residue separation and purification integration machine |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510597680.4A CN105238556A (en) | 2015-09-20 | 2015-09-20 | Centrifuged oil residue separation and purification integration machine |
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| CN105238556A true CN105238556A (en) | 2016-01-13 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201510597680.4A Pending CN105238556A (en) | 2015-09-20 | 2015-09-20 | Centrifuged oil residue separation and purification integration machine |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105689361A (en) * | 2016-03-08 | 2016-06-22 | 福建省迅达石化工程有限公司 | Device for separating organic sediment and water in deposited oil residues from inorganic sediment in deposited oil residues |
| CN105886150A (en) * | 2016-04-29 | 2016-08-24 | 镇江威孚锅炉有限公司 | Boiler descaling agent and preparation process thereof |
| CN106746148A (en) * | 2017-03-17 | 2017-05-31 | 成都源蓉科技有限公司 | A kind of magnetic loading precipitation filtration, purification system |
-
2015
- 2015-09-20 CN CN201510597680.4A patent/CN105238556A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105689361A (en) * | 2016-03-08 | 2016-06-22 | 福建省迅达石化工程有限公司 | Device for separating organic sediment and water in deposited oil residues from inorganic sediment in deposited oil residues |
| CN105689361B (en) * | 2016-03-08 | 2018-05-15 | 福建省迅达石化工程有限公司 | By the organogenous sediment and water device separated with inorganic sediment in the dregs of fat that deposit |
| CN105886150A (en) * | 2016-04-29 | 2016-08-24 | 镇江威孚锅炉有限公司 | Boiler descaling agent and preparation process thereof |
| CN106746148A (en) * | 2017-03-17 | 2017-05-31 | 成都源蓉科技有限公司 | A kind of magnetic loading precipitation filtration, purification system |
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