CN208327842U - A kind of integrated preparation facilities of load-type zero-valent iron porcelain ball - Google Patents

A kind of integrated preparation facilities of load-type zero-valent iron porcelain ball Download PDF

Info

Publication number
CN208327842U
CN208327842U CN201820789067.1U CN201820789067U CN208327842U CN 208327842 U CN208327842 U CN 208327842U CN 201820789067 U CN201820789067 U CN 201820789067U CN 208327842 U CN208327842 U CN 208327842U
Authority
CN
China
Prior art keywords
pipe
valve
valent iron
tube
load
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.)
Active
Application number
CN201820789067.1U
Other languages
Chinese (zh)
Inventor
宋诚
刘鸿
王厦
黄秋云
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.)
Chongqing Institute of Green and Intelligent Technology of CAS
Original Assignee
Chongqing Institute of Green and Intelligent Technology of CAS
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 Chongqing Institute of Green and Intelligent Technology of CAS filed Critical Chongqing Institute of Green and Intelligent Technology of CAS
Priority to CN201820789067.1U priority Critical patent/CN208327842U/en
Application granted granted Critical
Publication of CN208327842U publication Critical patent/CN208327842U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

The utility model belongs to technical field of material, it is related to a kind of integrated preparation facilities of load-type zero-valent iron porcelain ball, the first parametric measurement pipe that successively installation has regulating valve and communicates with solution allocation device on the first parameter regulation device at the top of solution allocation device, acid-base accommodation pipe, first air inlet pipe, first feed pipe, exhaust pipe and exhaust water pipe, solution allocation device bottom outside is equipped with the first evacuated tube with regulating valve, the second air inlet pipe that successively installation has regulating valve and communicates with material preparing device on the second parameter regulation device at the top of material preparing device, inlet tube, second feed pipe, second parametric measurement pipe and escape pipe, second air inlet pipe is communicated with inlet tube and is connected in the butt joint of exhaust water pipe one end by gas-liquid attachment device, material preparing device bottom outside is equipped with the second evacuated tube with regulating valve, it solves existing Reactor is essentially all the design carried out for the problem that powder Zero-valent Iron, is not suitable for load-type zero-valent iron porcelain ball.

Description

A kind of integrated preparation facilities of load-type zero-valent iron porcelain ball
Technical field
The utility model belongs to technical field of material, is related to a kind of standby dress of integration system of load-type zero-valent iron porcelain ball It sets more particularly to a kind of suitable load-type zero-valent iron synthesis, nano zero valence iron synthesizes and need to completely cut off air in the synthesis process Or need to prepare the reactor of material under certain atmosphere.
Background technique
Zero-valent Iron has excellent electrochemistry, Coordinative Chemistry and redox characteristic, with high reaction activity and application Range is wide, is a kind of environmentally friendly ecological environment repair materials.Result of study shows: Zero-valent Iron is heavy metal-polluted in solution environment There is superior performance, especially in processing high poison in terms of the environmental problems such as dye, debirs pollution and underground Water Ecological Recovery Property and difficult biochemical and conventional sewage processing method be difficult to have good prospect in terms of the heavy metal effectively degraded.Zero-valent Iron reaction It usually carries out at normal temperatures and pressures, with low energy consumption, non-selectivity high-efficient to contaminant degradation, can degrade a variety of dirts simultaneously The features such as contaminating object, therefore, Zero-valent Iron reduction technique by be a kind of great standby application prospect environmental improvement means.
Concern with people to environmental problem, the research about the preparation of Zero-valent Iron, modification and application aspect is increasingly Hot topic, however, the reproducibility of Zero-valent Iron is very strong, chemical property is extremely unstable, and easily occurs to reunite, is easily oxidized and loses Activity is difficult to prepare the zeroth order iron material that not only purity is high, activity are strong but also easy to maintain, limits its pushing away in terms of environment remediation Wide application.People begin trying to load to Zero-valent Iron on various media, then carry out using wherein load-type zero-valent iron porcelain ball is A kind of embedding Zero-valent Iron sphere uses load-type zero-valent iron porcelain ball as filler, due to its peculiar sphere shape of Zero-valent Iron porcelain ball And meso-hole structure, the Zero-valent Iron for participating in reduction conversion are internally contacted with pollutant when going deep into from porcelain ball surface, are gradually carried out Reduction conversion, most of Fe that this process is formed2+And Fe3+It being deposited inside porcelain ball, few part enters water body with ionic state, Fe2+Secondary reduction, the Fe of generation can be carried out to the pollutant in water body3+Coagulating sedimentation degradation can be carried out to water body, reach secondary The purpose of purifying water body.However existing reactor is essentially all to have certain limitation for powder Zero-valent Iron reaction designing Property to not applicable load-type zero-valent iron porcelain ball, in order to improve load-type zero-valent iron reduction conversion capability, reduction is reunited, and Easily recycling, is easily separated by solid-liquid separation, it is necessary to which reaction can either effectively be controlled by designing one kind for load-type zero-valent iron porcelain ball Process, while facilitating the novel reactor of experimental implementation again.Reactor design will solve the problems, such as it is that should completely cut off air, control PH, DO of reaction, time, improve the operability of charging, discharging again, while having simple structure and convenient processing, cost The advantages that low, safe and reliable, solve present reactor cannot continuously prepare, easily contact with air, low efficiency, nitrogen usage amount it is big The problems such as, solid foundation is provided for promotion and application of the load-type zero-valent iron porcelain ball in environment remediation.
Utility model content
In view of this, the utility model is essentially all to carry out for powder Zero-valent Iron to solve existing reactor The problem of design, unsuitable load-type zero-valent iron porcelain ball, provide a kind of integrated preparation facilities of load-type zero-valent iron porcelain ball.
In order to achieve the above objectives, the utility model provides a kind of integrated preparation facilities of load-type zero-valent iron porcelain ball, packet The solution allocation device and material preparing device of cylindrical shape are included,
Solution allocation device top side detachable is equipped with the first parameter regulation device of lid shape, on the first parameter regulation device Successively installation is with regulating valve and the first parametric measurement pipe communicated with solution allocation device, acid-base accommodation pipe, the first air inlet pipe, the One feed pipe, exhaust pipe and exhaust water pipe, the bottom of the first air inlet pipe is equipped between solution allocation device bottom that there are gaps The first sand core aeration tube, solution allocation device bottom outside be equipped with the first evacuated tube with regulating valve, exhaust water pipe one end insertion Below liquid level in solution allocation device, the other end is equipped with butt joint;
Material preparing device top side detachable is equipped with the second parameter regulation device of lid shape, on the second parameter regulation device Successively installation is with regulating valve and the second air inlet pipe communicated with material preparing device, inlet tube, the second feed pipe, the second parameter are surveyed Fixed pipe and escape pipe, the bottom of the second air inlet pipe are equipped between material preparing device bottom that there are second sand core in gap aerations Pipe, the second air inlet pipe are communicated with inlet tube and are connected in butt joint by gas-liquid attachment device, material preparing device bottom outside Equipped with the second evacuated tube with regulating valve.
Further, the first sand core aeration the distance between bottom of the tube aeration head and solution allocation device bottom for 0.5~ 1.5cm, it is 0.5~1.5cm that the second sand core, which is aerated the distance between bottom of the tube aeration head and material preparing device bottom,.
Further, solution allocation device and material preparing device upper outside are respectively equipped with the first external screw thread and the second external screw thread, It is respectively equipped on the inside of first parameter regulation device and the second parameter regulation device and is matched with the first external screw thread and the second external screw thread It is further respectively had on the inside of the first internal screw thread and the second internal screw thread used, the first parameter regulation device and the second parameter regulation device First sealing ring and the second sealing ring.
Further, solution allocation device and material preparing device material and size are all the same, and material is organic glass or polytetrafluoro Material, the height of solution allocation device and material preparing device: diameter=1.5~2.
Further, the first parametric measurement pipe, acid-base accommodation pipe, the first air inlet pipe, the first feed pipe, exhaust pipe and exhaust water It is respectively corresponded on pipe and the first parametric measurement pipe valve of monitoring data, the acid-base accommodation valve of antiacid caustic corrosion, the first air inlet is installed Valve, the first inlet valve, exhaust valve and the exhaust valve for adjusting gas-liquid amount.
Further, it is respectively corresponded on the second air inlet pipe, inlet tube, the second feed pipe, the second parametric measurement pipe and escape pipe Second intake valve, liquid feed valve, the second inlet valve, the second parametric measurement pipe valve and air outlet valve are installed.
Further, the first emptying valve for being equipped with antiacid alkali and second are respectively corresponded in the first evacuated tube and the second evacuated tube The diameter of exhaust-valve, the first evacuated tube and the second evacuated tube is 2~5cm.
Further, gas-liquid attachment device includes the soft silicone tube communicated with the second air inlet pipe with inlet tube, and soft silicone tube is remote One end from the second air inlet pipe and inlet tube is removably mounted in the butt joint of exhaust water pipe end, and change is equipped in butt joint Diameter device.
Further, it is 0.5~2cm that inlet tube, which protrudes into the distance in material preparing device,.
Further, the first graduated scale and the second graduated scale are respectively equipped on solution allocation device and material preparing device outer surface.
The utility model has the beneficial effects that:
The integrated preparation facilities of load-type zero-valent iron porcelain ball disclosed in the utility model, nitrogen pass through the first air inlet pipe Into solution allocation device, the air in solution allocation device is discharged, the solution materials of Zero-valent Iron porcelain ball will be prepared from cylindrical shape First feed pipe of solution allocation device enters in solution allocation device, so that being in nitrogen from the ferrous sulfate that the first feed pipe enters Protection atmosphere in, prevent ferrous sulfate to be oxidized.The solid material aluminum oxide microballoon of Zero-valent Iron porcelain ball is prepared from cylinder The second charging aperture of body shape material preparing device enters in material preparing device, is then being completely cut off solution materials by the pressure of nitrogen It is pressed onto material preparing device under conditions of air from solution allocation device, subsequent solution materials and solid material are in material preparing device Carry out the preparation of Zero-valent Iron porcelain ball;This preparation process whole process has nitrogen protection, zeroth order iron content in the Zero-valent Iron porcelain ball prepared Height is prepared into power height, and nitrogen usage amount is few, while nascent state Zero-valent Iron in preparation process being avoided rapidly to aoxidize.The Zero-valent Iron The production of porcelain ball integration preparation facilities is simple, easy to operate, can be used for that air need to be completely cut off or need the material under certain atmosphere Material preparation, solve present reactor Zero-valent Iron preparation content it is low, it is cumbersome, be not easy successfully, the problems such as nitrogen usage amount is big, It can be promoted and applied in environment remediation engineering.
Detailed description of the invention
In order to keep the purpose of this utility model, technical scheme and beneficial effects clearer, the utility model provides as follows Attached drawing is illustrated:
Fig. 1 is the integration system of the utility model load-type zero-valent iron porcelain ball for apparatus structure schematic diagram;
Fig. 2 is Zero-valent Iron porcelain ball SEM prepared by the integrated preparation facilities of the utility model load-type zero-valent iron porcelain ball Figure.
Specific embodiment
Below in conjunction with attached drawing, the preferred embodiment of the utility model is described in detail.
Appended drawing reference in Figure of description includes:
First feed pipe 1, the first inlet valve 2, the first intake valve 3, the first air inlet pipe 4, acid-base accommodation pipe 5, acid-base accommodation Valve 6, the first parametric measurement pipe 7, the first parametric measurement pipe valve 8, the first parameter regulation device 9, the first sealing ring 10, solution allocation Device 11, the first graduated scale 12, the first sand core aeration tube 13, first emptying valve 14, the first evacuated tube 15, exhaust valve 16, second Intake valve 17, the first external screw thread 18, the second external screw thread 19, the second graduated scale 20, the second air inlet pipe 21, the second sand core aeration tube 22, second emptying valve 23, the second evacuated tube 24, material preparing device 25, the second sealing ring 26, the second parameter regulation device 27, go out Air valve 28, escape pipe 29, the second parametric measurement pipe valve 30, the second parametric measurement pipe 31, the second inlet valve 32, the second feed pipe 33, liquid feed valve 34, inlet tube 35, gas-liquid attachment device 36, butt joint 37, exhaust water pipe 38, exhaust valve 39, exhaust pipe 40.
The integrated preparation facilities of load-type zero-valent iron porcelain ball as shown in Figure 1, the solution allocation device including cylindrical shape 11 and material preparing device 25, solution allocation device 11 and 25 material and size of material preparing device are all the same, and material is organic glass Or polytetrafluoro material, the height and diameter ratio of solution allocation device 11 and material preparing device 25 are 1.5~2,11 He of solution allocation device Material preparing device 25 is of moderate size.Solution allocation device 11 and material preparing device are respectively equipped with the first graduated scale 12 on 25 outer surface With the second graduated scale 20, ferrous sulfate and aluminum oxide microballoon can be observed by the first graduated scale 12 and the second graduated scale 20 The amount being separately added into solution allocation device 11 and material preparing device 25.
11 upper outside of solution allocation device is equipped with the first external screw thread 18, is equipped with and first on the inside of the first parameter regulation device 9 The first internal screw thread and the first sealing ring 10 that external screw thread 18 is used in combination.Pass through the first internal screw thread, the first sealing ring 10 and First parameter regulation device 9 can be fixedly mounted on 11 top of solution allocation device by the cooperation of one external screw thread 18.
The first parametric measurement pipe 7, the soda acid tune communicated with solution allocation device 11 is successively installed on the first parameter regulation device 9 Save pipe 5, the first air inlet pipe 4, the first feed pipe 1, exhaust pipe 40 and exhaust water pipe 38, the first parametric measurement pipe 7, acid-base accommodation pipe 5, it is respectively corresponded on the first air inlet pipe 4, the first feed pipe 1, exhaust pipe 40 and exhaust water pipe 38 and monitoring pH, DO, temperature is installed Etc. the first parametric measurement pipe valve 8 of data, the acid-base accommodation valve 6 of antiacid caustic corrosion, the first intake valve 3, the first inlet valve 2, row Air valve 39 and the exhaust valve 16 for adjusting gas-liquid amount.The first intake valve 3 in first air inlet pipe 4 is adjustable into solution allocation The regulating valve of 11 tolerance of device.Exhaust valve 39 on exhaust pipe 40 is also the regulating valve that can control discharge tolerance.First air inlet pipe 4 Bottom the first sand core aeration tube 13 between 11 bottom of solution allocation device there are gap, the first sand core aeration tube 13 are installed The distance between bottom aeration head and 11 bottom of solution allocation device are 0.5~1.5cm, and 11 bottom outside of solution allocation device is equipped with band First evacuated tube 15 of regulating valve is equipped with the first emptying valve 14 of antiacid alkali in the first evacuated tube 15, the first evacuated tube 15 Diameter is 2~5cm.It is vented below the liquid level in 38 one end of water pipe insertion solution allocation device 11, other end installation band variable diameter fills The butt joint 37 set.
25 upper outside of material preparing device is equipped with the second external screw thread 19, is equipped with and second on the inside of the second parameter regulation device 27 The second internal screw thread and the second sealing ring 26 that external screw thread 19 is used in combination.Pass through the second internal screw thread, the second sealing ring 26 and Second parameter regulation device 27 can be fixedly mounted on 25 top of material preparing device by the cooperation of two external screw threads 19.
The second air inlet that successively installation has regulating valve and communicates with material preparing device 25 on second parameter regulation device 27 Pipe 21, inlet tube 35, the second feed pipe 33, the second parametric measurement pipe 31 and escape pipe 29, the second air inlet pipe 21, inlet tube 35, It is respectively corresponded on second feed pipe 33, the second parametric measurement pipe 31 and escape pipe 29 and second intake valve 17, the corruption of antiacid alkali is installed The the second parametric measurement pipe valve 30 and antiacid alkali of the data such as the liquid feed valve 34 of erosion, the second inlet valve 32, monitoring pH, DO, temperature are rotten The air outlet valve 28 of erosion.It is 0.5~2cm that inlet tube 35, which protrudes into the distance in material preparing device 25,.Pacify the bottom of second air inlet pipe 21 Equipped with the second sand core aeration tube 22 between 25 bottom of material preparing device there are gap, 22 bottom of the second sand core aeration tube aeration The distance between head and 25 bottom of material preparing device are 0.5~1.5cm.Second air inlet pipe 21 communicates with inlet tube 35 and passes through gas Liquid attachment device 36 is connected in butt joint 37, and gas-liquid attachment device 36 includes communicating with the second air inlet pipe 21 and inlet tube 35 Soft silicone tube, soft silicone tube are removably mounted at exhaust 38 end of water pipe far from one end of the second air inlet pipe 21 and inlet tube 35 In butt joint 37, diameter changing device is installed in butt joint 37, butt joint 37 is enabled to be suitable for the soft silicone tube of different-diameter Connection.Soft silicone tube is connected to after being connected to the second air inlet pipe 21 with inlet tube 35 by pipeline butt joint 37 and exhaust water pipe 38 Together.25 bottom outside of material preparing device is equipped with the second evacuated tube 24 with regulating valve, is equipped in the second evacuated tube 24 antiacid The diameter of the second emptying valve 23 of alkali, the second evacuated tube 24 is 2~5cm.
When the integrated preparation facilities work of the load-type zero-valent iron porcelain ball, it is first turned on the first air inlet in solution dispenser The first intake valve 3 and exhaust valve 39 on pipe 4 and exhaust pipe 40 close the first parametric measurement pipe valve 8, acid in solution dispenser Alkali regulating valve 6, the first inlet valve 2, exhaust valve 16, first emptying valve 14, to the first air inlet pipe 4 with the rate of 100mL/min It is passed through nitrogen.The second intake valve 17, the air outlet valve 28 that exhaust valve 16 and material preparing device 25 are opened after 2min, simultaneously close off molten Liquid feed valve 34, the second inlet valve 32, the second parametric measurement pipe valve 30 on the exhaust valve 39 and material preparing device 25 of liquid dispenser With second emptying valve 23, continues after leading to nitrogen 2min to the first air inlet pipe 4 with the rate of 100mL/min, close material preparing device The second intake valve 17 and air outlet valve 28 on 25.Then exhaust valve 39, the first inlet valve 2 on solution allocation device 11 are opened, to Added in first feed pipe 1 and close the first inlet valve 2 that solution is prepared after 500mL level-one water, continue to the first air inlet pipe 4 with The rate of 100mL/min leads to nitrogen 5min or so, opens the first parametric measurement pipe valve 8 in solution dispenser, and measurement solution is matched The DO value of level-one water in device processed is closed the first parametric measurement pipe valve 8 in solution dispenser, is beaten when DO value is less than 0.2mg/L The second inlet valve 32 and the acid-base accommodation valve 6 in solution dispenser are opened, 27.8g ferrous sulfate is added from the first feed pipe 1, The 1+1 sulfuric acid that the ratio between water and bright sulfur acid volume are 1: 1 is added in acid-base accommodation pipe 5, pH value of solution is adjusted to 2 or so, closes the One inlet valve 2 and acid-base accommodation valve 6 then proceed to lead to nitrogen 2min to the first air inlet pipe 4 with the rate of 100mL/min.It opens 100g aluminum oxide microballoon is added in the second inlet valve 32 on material preparing device 25 from the second feed pipe 33, closes material The second inlet valve 32 on preparing device 25 opens liquid feed valve 34, air outlet valve 28 on material preparing device 25, closes solution dispenser On air outlet valve 28, prepared anaerobic ferrous sulfate solution is pressed by material preparing device 25 by the pressure of nitrogen at this time In, the second intake valve 17 on material preparing device 25 is opened, liquid feed valve 34 is closed, leads to nitrogen 5min, to aluminum oxide microballoon After air in duct is caught up with to the greatest extent, the second parametric measurement pipe valve 30 in material preparing device 25 is opened, DO to be determined is less than Material is closed after 0.2mg/L and prepares upper second parametric measurement pipe valve 30, air outlet valve 28 and the second intake valve 17, is closed solution and is prepared The first intake valve 3 on device stops logical nitrogen.
After aluminum oxide microballoon adsorbs 6h, the also docking between openable exhaust water pipe 38 and gas-liquid attachment device 36 First 37, material preparing device 25 is put into oscillator, to connect butt joint 37 after the rate oscillation 6h of 150rd/min.Matched with solution Device processed prepares anaerobic water, then opens the second emptying valve 23 of material preparing device 25, closes second emptying valve 23 after emptying solution, Anaerobic water in solution preparing device nitrogen is pressed into material preparing device 25, Zero-valent Iron microballoon 3 is washed under the protection of nitrogen It is secondary, then washed twice with dehydrated alcohol, open the second parameter regulation device 27 on material preparing device 25, the zeroth order that will be prepared Iron microballoon be transferred in container place it is dry in vacuum desiccator, be sealed after dry it is spare, through scanning electron microscopic observation, preparation Zero-valent Iron diameter in good Zero-valent Iron microballoon as shown in Figure 2 duct is in 100nm or so, and zeroth order iron content is 98% or so.
Finally, it is stated that preferred embodiment above is merely intended for describing the technical solutions of the present application, but not for limiting the present application, to the greatest extent Pipe has been described in detail the utility model by above preferred embodiment, but those skilled in the art should manage Solution, can make various changes, without departing from the utility model claims book institute to it in the form and details The range of restriction.

Claims (10)

1. a kind of integrated preparation facilities of load-type zero-valent iron porcelain ball, which is characterized in that the solution allocation including cylindrical shape Device and material preparing device,
The solution allocation device top side detachable is equipped with the first parameter regulation device of lid shape, the first parameter regulation dress Set the first parametric measurement pipe, the acid-base accommodation pipe, the first air inlet that successively installation has regulating valve and communicates with solution allocation device Pipe, the first feed pipe, exhaust pipe and exhaust water pipe, the bottom of first air inlet pipe is equipped between solution allocation device bottom There are the first sand core aeration tube in gap, the solution allocation device bottom outside is equipped with the first evacuated tube with regulating valve, described It is vented below the liquid level in water pipe one end insertion solution allocation device, the other end is equipped with butt joint;
The material preparing device top side detachable is equipped with the second parameter regulation device of lid shape, the second parameter regulation dress Successively installation is set with regulating valve and the second air inlet pipe communicated with material preparing device, inlet tube, the second feed pipe, the second ginseng Number measurement pipe and escape pipe, the bottom of second air inlet pipe are equipped between material preparing device bottom that there are the second of gap Sand core aeration tube, second air inlet pipe are communicated with inlet tube and are connected in butt joint by gas-liquid attachment device, the material Expect that preparing device bottom outside is equipped with the second evacuated tube with regulating valve.
2. the integrated preparation facilities of load-type zero-valent iron porcelain ball as described in claim 1, which is characterized in that first sand core Being aerated the distance between bottom of the tube aeration head and solution allocation device bottom is 0.5~1.5cm, and the second sand core is aerated bottom of the tube aeration The distance between head and material preparing device bottom are 0.5~1.5cm.
3. the integrated preparation facilities of load-type zero-valent iron porcelain ball as claimed in claim 2, which is characterized in that the solution allocation Device and material preparing device upper outside are respectively equipped with the first external screw thread and the second external screw thread, the first parameter regulation device and The first internal screw thread being used in combination with the first external screw thread and the second external screw thread and the are respectively equipped on the inside of two parameter regulation devices The first sealing ring and the second sealing are further respectively had on the inside of two internal screw threads, the first parameter regulation device and the second parameter regulation device Circle.
4. the integrated preparation facilities of load-type zero-valent iron porcelain ball as claimed in claim 2, which is characterized in that the solution allocation Device and material preparing device material and size are all the same, and material is organic glass or polytetrafluoro material, solution allocation device and material system The height of standby device: diameter=1.5~2.
5. the integrated preparation facilities of load-type zero-valent iron porcelain ball as described in Claims 1 to 4 is any, which is characterized in that described Peace is respectively corresponded on first parametric measurement pipe, acid-base accommodation pipe, the first air inlet pipe, the first feed pipe, exhaust pipe and exhaust water pipe The acid-base accommodation valve of the first parametric measurement pipe valve, antiacid caustic corrosion equipped with monitoring data, the first intake valve, the first inlet valve, Exhaust valve and the exhaust valve for adjusting gas-liquid amount.
6. the integrated preparation facilities of load-type zero-valent iron porcelain ball as claimed in claim 5, which is characterized in that second air inlet Respectively corresponded on pipe, inlet tube, the second feed pipe, the second parametric measurement pipe and escape pipe be equipped with the second intake valve, liquid feed valve, Second inlet valve, the second parametric measurement pipe valve and air outlet valve.
7. the integrated preparation facilities of load-type zero-valent iron porcelain ball as claimed in claim 6, which is characterized in that first emptying The first emptying valve and second emptying valve for being equipped with antiacid alkali, the first evacuated tube and second are respectively corresponded in pipe and the second evacuated tube The diameter of evacuated tube is 2~5cm.
8. the integrated preparation facilities of load-type zero-valent iron porcelain ball as claimed in claim 7, which is characterized in that the gas-liquid connection Device includes the soft silicone tube communicated with the second air inlet pipe with inlet tube, soft silicone tube far from the second air inlet pipe and inlet tube one End is removably mounted in the butt joint of exhaust water pipe end, is equipped with diameter changing device in the butt joint.
9. the integrated preparation facilities of load-type zero-valent iron porcelain ball as claimed in claim 8, which is characterized in that the inlet tube is stretched Entering the distance in material preparing device is 0.5~2cm.
10. the integrated preparation facilities of load-type zero-valent iron porcelain ball as claimed in claim 9, which is characterized in that the solution is matched It sets and is respectively equipped with the first graduated scale and the second graduated scale on device and material preparing device outer surface.
CN201820789067.1U 2018-05-24 2018-05-24 A kind of integrated preparation facilities of load-type zero-valent iron porcelain ball Active CN208327842U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820789067.1U CN208327842U (en) 2018-05-24 2018-05-24 A kind of integrated preparation facilities of load-type zero-valent iron porcelain ball

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820789067.1U CN208327842U (en) 2018-05-24 2018-05-24 A kind of integrated preparation facilities of load-type zero-valent iron porcelain ball

Publications (1)

Publication Number Publication Date
CN208327842U true CN208327842U (en) 2019-01-04

Family

ID=64775044

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820789067.1U Active CN208327842U (en) 2018-05-24 2018-05-24 A kind of integrated preparation facilities of load-type zero-valent iron porcelain ball

Country Status (1)

Country Link
CN (1) CN208327842U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109841884A (en) * 2019-04-04 2019-06-04 中国科学院重庆绿色智能技术研究院 A kind of microbiological fuel cell liquid changing device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109841884A (en) * 2019-04-04 2019-06-04 中国科学院重庆绿色智能技术研究院 A kind of microbiological fuel cell liquid changing device
CN109841884B (en) * 2019-04-04 2024-10-18 中国科学院重庆绿色智能技术研究院 Liquid changing device of microbial fuel cell

Similar Documents

Publication Publication Date Title
CN208327842U (en) A kind of integrated preparation facilities of load-type zero-valent iron porcelain ball
CN203641589U (en) Combined-type energy-saving water-sealed valve
CN209383677U (en) A kind of fertilizer installation for fermenting
CN219324054U (en) Multifunctional biogas purifying device
CN201212616Y (en) Leakage treating device of gas tank
CN208542173U (en) A kind of preparation facilities of load-type zero-valent iron porcelain ball
CN206204075U (en) A kind of light catalytic waste water processing device
CN208825547U (en) Superfine aluminium power surface modifying apparatus
CN201419093Y (en) Novel reaction vessel
CN107195868A (en) A kind of sulphur anode composite material preparation facilities and control method based on sodium thiosulfate and acid reaction
CN102228771A (en) Polysilicon tail gas processing method
CN112897460A (en) Portable hydrogen production reactor
CN204778972U (en) Whirl electrolysis flocculation plant
CN211896834U (en) Blast furnace gas desulphurization device
CN206375667U (en) Device for producing hydrogen
CN105820832B (en) Electrochemical catalysis normal temperature and pressure diesel oil desulfurization method
CN221777795U (en) Methane dry-method filtering desulfurization device
CN209481602U (en) A kind of dewatering desulfurizer for thick biogas
CN209619300U (en) A kind of biogas pre-processing device
CN209333487U (en) It is a kind of for producing the desulfurizer of tungsten disulfide exhaust-gas treatment
CN213492965U (en) Novel adsorption oxidation deodorization device
CN215828395U (en) Gallium adsorption device in electrolysis tail liquid
CN114524410A (en) Dropping liquid hydrogen producing process and device
CN221370836U (en) Efficient ABR anaerobic reactor
CN206368060U (en) A kind of water process hydroxyl generator

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant