CN104193563A - Paddle-free mixing device for mechanosensitive explosives and powders - Google Patents

Paddle-free mixing device for mechanosensitive explosives and powders Download PDF

Info

Publication number
CN104193563A
CN104193563A CN201410421146.3A CN201410421146A CN104193563A CN 104193563 A CN104193563 A CN 104193563A CN 201410421146 A CN201410421146 A CN 201410421146A CN 104193563 A CN104193563 A CN 104193563A
Authority
CN
China
Prior art keywords
mixing
mixing kettle
kettle
spray tube
diameter
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201410421146.3A
Other languages
Chinese (zh)
Other versions
CN104193563B (en
Inventor
马宁
陈松
秦能
张亮
陈�基
刘晶
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.)
Xian Modern Chemistry Research Institute
Original Assignee
Xian Modern Chemistry Research Institute
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 Xian Modern Chemistry Research Institute filed Critical Xian Modern Chemistry Research Institute
Priority to CN201410421146.3A priority Critical patent/CN104193563B/en
Publication of CN104193563A publication Critical patent/CN104193563A/en
Application granted granted Critical
Publication of CN104193563B publication Critical patent/CN104193563B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention discloses a paddle-free mixing device for mechanosensitive explosives and powders, which solves the problem of uniformly mixing a material with the mechanosensitive explosives and powders. The device comprises a mixing kettle (1), a kettle cover (2), an isolating kettle (3), a gas distributor (4), an injection pipe (5) and a nozzle (6). The device has the characteristics of being adjustable in elements, controllable in severe degree, small in vibration, convenient to maintain and free from mechanical shear and gas protection can be introduced, and is suitable for mixing the mechanosensitive explosives and powders, particularly mixing the explosives and powders of a long fiber material which is easy to be mechanically shared and damaged.

Description

A kind of mechanical sensitivity fire explosive is without oar mixing device
Technical field
The invention belongs to fiery explosive hybrid technique technical field, relate to a kind of mechanical sensitivity fire explosive without oar mixing device, be specifically related to a kind of device containing the fiery explosive of long fiber material that can be adapted to mix.
Background technology
Hybrid technique is that fiery explosive field mutually disperses two or more materials and reaches the indispensable important process technology of certain degree of uniformity, is the important factor of the fiery explosive product performance of impact.Common hybrid mode is uniformly mixed, mediates mixing, rotating cylinder mixing, filter screen mixing, ultrasonic mixing etc.Wherein ultrasonic mixing and filter screen are blended in fiery Explosive Industry and rarely have application.What fire explosive field was most widely used is exactly to be uniformly mixed, to mediate to mix and rotating cylinder mixing, and rotating cylinder mixing drives materials inside rolling to realize dispersion mutually by rotating cylinder, is used for admittedly mixing; Kneading is mixed for the mixing of the viscoelastic body of a large amount of solids and a small amount of liquid composition; Be uniformly mixed for solid-liquid mixing, liquid liquid and mix and gas-liquid mixed.Wherein mediating the ultimate principle of mixing and being uniformly mixed is to utilize blade to mix effects such as the mechanical shearing of material, stretchings.
In fiery explosive field, some matrix material is in order to realize certain functional requirement, in formula, add appropriate long fiber material, the geometrical shape of these materials, size are through the definite optimum shape dimensional parameters of experimental formula repeatedly, are determining the performance of matrix material.But the easy stressed generation deformation of these filamentary materials or fracture, affect its role in matrix material.Therefore, how to guarantee that homogenization that long fiber material physical condition do not change disperses to become the gordian technique place of composite processing.In conventional hybrid mode, mediating mixing is to realize macrofiber dispersed comparatively desirable means in matrix material, but its strong shearing and stretching action can make the shape and size of long fiber material by considerable damage, thereby affects its proper property.At the first stage of composite processing, first make long fiber material dispersed in liquid phase formula, be the favorable method that reduces its structure deteriorate.But the mode that is uniformly mixed of mixing for fiery explosive field solid-liquid can produce and clashes into and shear long fiber material, make its fracture, and long fiber material is as easy as rolling off a log becomes entangled on stirring rake and stir shaft, is difficult to realize dispersed object.
Summary of the invention
One of object of the present invention be to overcome the deficiency of prior art and provide a kind of mixing device element adjustable, mix violent degree controlled, vibrate little, easy to maintenance, machinery-free is sheared, can introduce gas shield be applicable to mechanical sensitivity fire explosive without oar mixing device.
Object of the present invention can be achieved through the following technical solutions: a kind of mechanical sensitivity fire explosive is without oar mixing device, and this device comprises mixing kettle, kettle cover, isolation still, gas distributor, spray tube, nozzle; Mixing kettle bottom is provided with discharge port, and kettle cover is provided with opening for feed, the air inlet mouth of pipe and exhaust pipe mouth, and isolation still is provided with nozzle open holes and discharge port, and gas distributor is provided with the air inlet mouth of pipe, and spray tube is provided with nozzle open holes and drain, and nozzle is provided with pore.
The nominal diameter of mixing kettle is not more than 700mm, and mixing kettle aspect ratio is 1~1.5: 1, and coefficient is 0.6~0.8, mixing kettle lower surface adopts normal ellipsoidal head, upper end is uncovered and outward flange is set, and mixing kettle discharge port is located at lower cover center position, diameter 30~50mm.
Isolation still profile and mixing kettle are in full accord, diameter and be highly all less than mixing kettle, wherein external diameter is the poor of mixing kettle internal diameter and spray tube diameter, and top is uncovered, isolation still wall and lower cover have open holes, at the bottom of still, have discharge port, it is identical that discharge port diameter and mixing kettle are opened discharge port diameter, is 30~50mm.
Spray tube structurally consists of two portions, a part is for pasting the injection arm of mixing kettle inwall and isolation still outer wall, another part is the ring pipe coaxial with mixing kettle, spraying arm is 50~200mm at the part separation parallel with mixing kettle straight cylinder bus, final all injection arms intersect at ring pipe, and ring pipe central diameter is 100~200mm.Below charging liquid level, spray tube arranges nozzle open holes, be spaced apart 50~100mm, oblique lower 45 ° of aperture, on segmental arc top, arrange nozzle open holes, aperture direction is vertically pointed to mixing kettle axis, arranges nozzle open holes on ring pipe, and aperture is directed upwardly and parallel mixing still axis.With ring pipe concentric, diameter is that nozzle open holess are arranged in 1.5~3 times of ring pipe central diameter annulus positions, aperture is directed upwardly parallel mixing still axis.Symmetrical 2 drains of ring pipe lowermost end, diameter is 2~5mm, sprays arm operative tip and is processed into inner groovy form.
Gas distributor is comprised of a female groove and a series of distribution arms, and distribution arms one end connects female groove, and one end is processed into outer form of grooves, and distribution arms quantity is consistent with injection arm with caliber, and female groove upper end is provided with air inlet port.
Nozzle one end is connected with spray tube, and the other end arranges flat head, ventilate on flat head, and pore opening is 0.5~2mm, and the shared flat head area ratio of pore is not less than 0.5, and pore opening and density are according to the viscosity-modifying of mixing liquid.
Mixing process is gases used can select pressurized air, compressed nitrogen or other rare gas elementes according to material characteristic.
Compared with prior art, feature of the present invention is: mixing device element is adjustable, the violent degree of mixing is controlled, it is little, easy to maintenance to vibrate, machinery-free is sheared, can be introduced gas shield.This mixing device can be realized the even mixing containing long fiber material fire explosive, compares with conventional hybrid mode, and mixing process reduces by 40% to the destructive rate of long fiber material shape and size.This mixing device can be changed nozzle flexibly according to the physical attribute of blending objects and mutual ratio.This mixing device can prevent from producing and being wound around in the rotation of long fiber material in mixing kettle or attachment mechanism.
Accompanying drawing explanation
Fig. 1 is that a kind of mechanical sensitivity fire explosive of the present invention is without the structural representation of oar mixing device.
Fig. 2 is gas distributor structural representation of the present invention.
Fig. 3 is spray tube structural representation of the present invention.
Fig. 4 is nozzle face schematic diagram of the present invention.
1 mixing kettle, 2 kettle covers, 3 isolation stills, 4 gas distributors, 5 spray tubes, 6 nozzles, 7 open holess, 8 isolation still discharge ports, 9 mixing kettle discharge ports, 10 opening for feeds, 11 venting holes, 12 kettle cover air inlet ports, 13 sparger air inlet ports, 14 female grooves, 15 distribution arms, 16 outer grooves, 17 inner groovies, 18 nozzle open holess, 19 ring pipes, 20 spray arm, 21 drains, 22 flat heads, 23 pores.
Embodiment
Below in conjunction with Figure of description, the present invention will be further described.
As shown in Figures 1 to 4, a kind of mechanical sensitivity fire explosive of the present invention comprises mixing kettle 1, kettle cover 2, isolation still 3, gas distributor 4, spray tube 5, nozzle 6 without oar mixing device.The concrete structure of gas distributor 4 is shown in Fig. 2, and the concrete structure of spray tube 5 is shown in Fig. 3, and the end face structure of nozzle 6 is shown in Fig. 4.
The nominal diameter of described mixing kettle 1 is not more than 700mm, mixing kettle 1 aspect ratio is 1~1.5: 1, coefficient is 0.6~0.8, mixing kettle 1 lower surface adopts normal ellipsoidal head, upper end is uncovered and outward flange is set, flange and kettle cover 2 are bolted, and the discharge port 9 of mixing kettle 1 is located at lower cover center position, and diameter is 30~50mm.Mixing kettle 1 is that a kind of mechanical sensitivity fire explosive is without the pressure-bearing part of oar mixing device.
On described kettle cover 2, open three holes, be respectively opening for feed 10, venting port 11, inlet mouth 12, opening for feed 10 and quantifying feed equipment connection, arrange back pressure valve in associated pipe; Venting port 11 is connected with induced draft fan, and inlet mouth 12 is connected with compression gas tank, for pressurized gas, enters gas distributor 4.
Described isolation still 3 profiles and mixing kettle 1 are in full accord, diameter and be highly less than mixing kettle 1, wherein external diameter is the poor of mixing kettle 1 internal diameter and spray tube 5 external diameters, and top is uncovered, after installing gas sparger 4 and spray tube 5, can be close to gas distributor 4 and spray tube 5, isolation still 3 has open holes 7, and isolation still 3 centers, bottom have discharge port 8, discharge port 8 diameters are identical with mixing kettle 1 discharge port of opening 9 diameter, are 30~50mm.Isolation still 3 is mainly used in fixedly spray tube 5, installation nozzle 6, prevents that the macrofiber in mixture from stopping up or being wound around in the gap of spray tube 5.
As depicted in figs. 1 and 2, described gas distributor 4 is comprised of a female groove 14 and a series of distribution arms 15, distribution arms 15 one end connect female groove 14, one end is processed into outer groove 16, gas distributor 4 tops have inlet mouth 13, this inlet mouth 13 is in the same size with the inlet mouth 12 on kettle cover 2, all has internal thread, is connected with inlet pipe.The quantity of distribution arms 15 is consistent with injection arm 20 with caliber.
As shown in figures 1 and 3, described spray tube 5 has nozzle open holes 18 at nozzle 6 installed positions, sprays arm 20 ingresss and is processed into inner groovy 17, and this inner groovy 17 assembles with the outer groove 16 of gas distributor 4, and centre is lined with plastics or rubber sheet gasket.Spray tube 5 top side nozzle open holess 18 should be lower than the in-built feed liquid face of mixing kettle 1, and nozzle open holes 18 directions are for vertically upward or oblique lower 45 °.Spray tube 5 ring pipe 19 part central diameters are 100~200mm, and open two drains 21 in ring pipe 19 position symmetries, for the liquid material emptying in spray tube after shutting down 5.Spray tube 5 can be changed flexibly according to the process requirements of concrete material.
As shown in Figure 1 and Figure 4, described nozzle 6 one end are connected with spray tube 5 by isolation still 3.Nozzle 6 one end arrange flat head 22, and on flat head 22, ventilate 23, and pore 23 sizes are 0.5~2mm, and pore 23 sizes and density are according to the viscosity-modifying of mixture, and shared end socket 22 area ratios of pore 23 are not less than 0.5.Nozzle 6 can be changed flexibly according to different material.
Erection sequence of the present invention is at the interior installation spray tube 5 of mixing kettle 1, and then isolation still 3 is installed, and then nozzle 6 is installed, and then installing gas sparger 4, and then kettle cover 2 is installed, and then other auxiliary setting and annex is installed.Un-mate sequence is contrary with erection sequence, disassembles front needs through fully wash and remove nozzle 6 under Soaking environment.Mixing process of the present invention jet flow stream used is used pressurized air, compressed nitrogen or other rare gas elementes according to mixed material property feature.

Claims (7)

1. a mechanical sensitivity fire explosive is without oar mixing device, by mixing kettle (1), kettle cover (2), isolation still (3), gas distributor (4), spray tube (5), nozzle (6), formed, it is characterized in that, described spray tube (5) is placed in mixing kettle (1), isolation still (3) is put into mixing kettle (1), coaxially, spray tube (5) is clipped in the middle of mixing kettle (1) and isolation still (3) for mixing kettle (1), spray tube (5), isolation still (3); Nozzle (6) is installed on spray tube (5) by open holes (7) and nozzle open holes (18); Gas distributor (4) is installed in mixing kettle (1), and the outer groove (16) on gas distributor (4) docks with the inner groovy (17) on spray tube (5); Kettle cover (2) is installed on mixing kettle (1) top, and connects with screw; Described mixing kettle (1) bottom is provided with discharge port (9); Described kettle cover (2) is provided with opening for feed (10), inlet mouth (12) and venting port (11); Described isolation still (3) profile is consistent with mixing kettle (1), is provided with open holes (7) and discharge port (8); Described spray tube (5) is comprised of ring pipe (19) and injection arm (20), is provided with nozzle open holes (18) and material drain (21); Described gas distributor (4) is comprised of female groove (14) and distribution arms (15), is provided with inlet mouth (13), and distribution arms (15) top is provided with outer groove (16); Described nozzle (6) has pore (23) on flat head (22).
2. a kind of mechanical sensitivity fire explosive according to claim 1 is without oar mixing device, it is characterized in that, the nominal diameter of described mixing kettle (1) is not more than 700mm, mixing kettle (1) aspect ratio is 1~1.5: 1, coefficient is 0.6~0.8, and mixing kettle (1) lower surface adopts normal ellipsoidal head, and upper end is uncovered and outward flange is set, mixing kettle (1) discharge port (9) is located at lower cover center position, diameter 30~50mm.
3. a kind of mechanical sensitivity fire explosive according to claim 1 is without oar mixing device, it is characterized in that, described isolation still (3) profile is consistent with mixing kettle (1), diameter and be highly all less than mixing kettle (1), wherein external diameter is the poor of mixing kettle (1) internal diameter and spray tube (5) diameter, and top is uncovered, isolation still (3) wall and lower cover have open holes (7), at the bottom of still, have discharge port (8), isolation still discharge port (8) diameter is identical with mixing kettle (1) discharge port of opening (9) diameter, is 30~50mm.
4. a kind of mechanical sensitivity fire explosive according to claim 1 is without oar mixing device, it is characterized in that, described spray tube (5) structurally consists of two portions, a part is for pasting the injection arm (20) of mixing kettle (1) inwall and isolation still (3) outer wall, another part is the ring pipe (19) coaxial with mixing kettle (1), spraying arm (20) is 50~200mm at the part separation parallel with mixing kettle (1) straight cylinder bus, all injection arms (20) intersect at ring pipe (19), and ring pipe (19) central diameter is 100~200mm; Below charging liquid level, spray tube (5) arranges nozzle open holes (18), be spaced apart 50~100mm, oblique lower 45 ° of aperture, on segmental arc top, arrange nozzle open holes (18), aperture direction is vertically pointed to mixing kettle (1) axis, and at the upper nozzle open holes (18) of arranging of ring pipe (19), aperture is directed upwardly and parallel mixing still (1) axis; With ring pipe (19) concentric, diameter is that 1.5~3 times of ring pipes (19) central diameter annulus position arranges that nozzle open holes (18), aperture are directed upwardly and parallel mixing still (1) axis; Symmetrical 2 drains of ring pipe (19) lowermost end (21), diameter is 2~5mm, sprays arm (20) top and is processed into inner groovy (17) form.
According to claim 1, a kind of mechanical sensitivity claimed in claim 4 fire explosive without oar mixing device, it is characterized in that, described gas distributor (4) is that distribution arms (15) forms by a female groove (14) and, distribution arms (15) one end connects female groove (14), one end is processed into outer groove (16) form, distribution arms (15) quantity is consistent with injection arm (20) with caliber, and female groove (14) upper end is provided with air inlet port (13).
According to claim 1, a kind of mechanical sensitivity claimed in claim 4 fire explosive without oar mixing device, it is characterized in that, described nozzle (6) one end is connected with spray tube (5), one end arranges flat head (22), the upper ventilate (23) of flat head (22), pore (23) size is 0.5~2mm, and the shared flat head of pore (23) (22) area ratio is not less than 0.5.
According to a kind of mechanical sensitivity fire of claim 1~claimed in claim 6 explosive without oar mixing device, it is characterized in that, described jet flow stream can be selected pressurized air, compressed nitrogen or other rare gas elementes according to material characteristic.
CN201410421146.3A 2014-08-25 2014-08-25 A kind of mechanical sensitivity explosive wastewater is without oar mixing arrangement Expired - Fee Related CN104193563B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410421146.3A CN104193563B (en) 2014-08-25 2014-08-25 A kind of mechanical sensitivity explosive wastewater is without oar mixing arrangement

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410421146.3A CN104193563B (en) 2014-08-25 2014-08-25 A kind of mechanical sensitivity explosive wastewater is without oar mixing arrangement

Publications (2)

Publication Number Publication Date
CN104193563A true CN104193563A (en) 2014-12-10
CN104193563B CN104193563B (en) 2016-09-14

Family

ID=52078979

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410421146.3A Expired - Fee Related CN104193563B (en) 2014-08-25 2014-08-25 A kind of mechanical sensitivity explosive wastewater is without oar mixing arrangement

Country Status (1)

Country Link
CN (1) CN104193563B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109123742A (en) * 2018-09-27 2019-01-04 杨成云 A kind of pipe tobacco and sheet and shreds are mixed with device and blending

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4209259A (en) * 1978-11-01 1980-06-24 Rains Robert L Magnetic mixer
CN2381636Y (en) * 1997-01-23 2000-06-07 杨祖一 Ultrafine pulverizing and mixing apparatus for solid explosive
RU2176229C1 (en) * 2000-09-26 2001-11-27 Государственное унитарное предприятие "Научно-исследовательский институт полимерных материалов" Mixing and moulding plant
RU2006100755A (en) * 2006-01-10 2007-07-27 Федеральное государственное унитарное предпри тие"Научно-исследовательский институт полимерных материалов" (RU) DEVICE FOR MIXING COMPONENTS OF EXPLOSIVE COMPOSITIONS AND PRESSING PRODUCTS FROM THEM
RU2310637C1 (en) * 2006-04-13 2007-11-20 Федеральное государственное унитарное предприятие "Научно-исследовательский институт полимерных материалов" Method of manufacturing a product from explosive composition
EP2138223A2 (en) * 2008-06-25 2009-12-30 CS Automazione S.r.l. Storage, mixing, homogenising and dosing group
CN102438796A (en) * 2009-05-15 2012-05-02 西姆佩尔坎普机械设备制造有限责任公司和两合公司 Method and apparatus for continuously mixing fibers with a binding agent
CN202224106U (en) * 2011-09-23 2012-05-23 北京厚德交通科技有限公司 Fiber mixing device
CN102489238A (en) * 2011-12-08 2012-06-13 中国石油化工股份有限公司 Efficient gas-liquid self-mixing reactor
CN202909644U (en) * 2012-11-08 2013-05-01 卜明 Non-stirring mixing device
CN103846038A (en) * 2012-11-29 2014-06-11 上海新力动力设备研究所 Anti-reversal paddle-free mixer
CN103851089A (en) * 2012-11-29 2014-06-11 上海新力动力设备研究所 Thrust sliding bearing part of paddle-free mixer

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4209259A (en) * 1978-11-01 1980-06-24 Rains Robert L Magnetic mixer
CN2381636Y (en) * 1997-01-23 2000-06-07 杨祖一 Ultrafine pulverizing and mixing apparatus for solid explosive
RU2176229C1 (en) * 2000-09-26 2001-11-27 Государственное унитарное предприятие "Научно-исследовательский институт полимерных материалов" Mixing and moulding plant
RU2006100755A (en) * 2006-01-10 2007-07-27 Федеральное государственное унитарное предпри тие"Научно-исследовательский институт полимерных материалов" (RU) DEVICE FOR MIXING COMPONENTS OF EXPLOSIVE COMPOSITIONS AND PRESSING PRODUCTS FROM THEM
RU2310637C1 (en) * 2006-04-13 2007-11-20 Федеральное государственное унитарное предприятие "Научно-исследовательский институт полимерных материалов" Method of manufacturing a product from explosive composition
EP2138223A2 (en) * 2008-06-25 2009-12-30 CS Automazione S.r.l. Storage, mixing, homogenising and dosing group
CN102438796A (en) * 2009-05-15 2012-05-02 西姆佩尔坎普机械设备制造有限责任公司和两合公司 Method and apparatus for continuously mixing fibers with a binding agent
CN202224106U (en) * 2011-09-23 2012-05-23 北京厚德交通科技有限公司 Fiber mixing device
CN102489238A (en) * 2011-12-08 2012-06-13 中国石油化工股份有限公司 Efficient gas-liquid self-mixing reactor
CN202909644U (en) * 2012-11-08 2013-05-01 卜明 Non-stirring mixing device
CN103846038A (en) * 2012-11-29 2014-06-11 上海新力动力设备研究所 Anti-reversal paddle-free mixer
CN103851089A (en) * 2012-11-29 2014-06-11 上海新力动力设备研究所 Thrust sliding bearing part of paddle-free mixer

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
万新斌: "无桨混合机中药浆流动规律实验研究", 《中国优秀硕士学位论文全文数据库》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109123742A (en) * 2018-09-27 2019-01-04 杨成云 A kind of pipe tobacco and sheet and shreds are mixed with device and blending

Also Published As

Publication number Publication date
CN104193563B (en) 2016-09-14

Similar Documents

Publication Publication Date Title
CN102674909B (en) Food waste hydrolysis and spray explosion system
CN204147810U (en) A kind of blender
CN204159286U (en) A kind of powder and apparatus for combining liquids
CN107115818B (en) Premixing device of chemical reaction kettle
CN101406865A (en) Spray finishing device for bi-component nano material
CN105729654A (en) Gas-assisted wet process mixing and preparing device for rubber
CN104193563A (en) Paddle-free mixing device for mechanosensitive explosives and powders
CN101531282B (en) Conveyer device for powder in micro-amount
CN205518309U (en) Double -barrelled spray gun
CN204848628U (en) Glass processing mixes and adds water installation
CN102556669B (en) Gas-solid mixing accelerating chamber
CN204973744U (en) Equal compounding device of double jet
CN209302644U (en) A kind of paint mixing equipment
CN203663766U (en) Humidifying airflow mixing machine
CN203196584U (en) Solid-liquid mixing tank
CN104958852A (en) Vertical foam generator
CN216024281U (en) Premix dry powder stirring equipment for fireproof paint production
CN209456323U (en) Admixture adding device is used in a kind of production of modified fast hydration engineering material
CN206716644U (en) Skinning cleaning plant
CN204429121U (en) For the connection device of gas-liquid mixed instrument
CN204864627U (en) Vertical foam generator
CN203196180U (en) Gas powder agitating device for fire extinguisher
CN217499191U (en) Pre-saccharification pot feeding system applied to beer industry
CN213669945U (en) Air humidifying device of carton workshop
CN210934681U (en) Water paint production is with raw materials feeding device

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160914

Termination date: 20190825

CF01 Termination of patent right due to non-payment of annual fee