CN1118280A - Fluid processing device - Google Patents

Fluid processing device Download PDF

Info

Publication number
CN1118280A
CN1118280A CN 94115657 CN94115657A CN1118280A CN 1118280 A CN1118280 A CN 1118280A CN 94115657 CN94115657 CN 94115657 CN 94115657 A CN94115657 A CN 94115657A CN 1118280 A CN1118280 A CN 1118280A
Authority
CN
China
Prior art keywords
hole
helix tube
filtration members
fluid
encapsulated
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
CN 94115657
Other languages
Chinese (zh)
Other versions
CN1063982C (en
Inventor
铃木旭
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.)
AICHISERAMIKKUKOGYOSYO
Original Assignee
AICHISERAMIKKUKOGYOSYO
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 AICHISERAMIKKUKOGYOSYO filed Critical AICHISERAMIKKUKOGYOSYO
Priority to CN94115657A priority Critical patent/CN1063982C/en
Publication of CN1118280A publication Critical patent/CN1118280A/en
Application granted granted Critical
Publication of CN1063982C publication Critical patent/CN1063982C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Abstract

The apparatus for such fluid treatments as purifying or activating water, improving oil quality, clarifying exhausted gas, and mixing water with fuel oil to obtain emulsified fuel has a spiral pipe with central through hole, a passage surrounding the said through hole, and a continuous porous filter in the said through hole, and features that even if the inlet of the filter is blocked, fluid may flow through the passage into the netted continuous porous filter.

Description

Fluid treating device
The present invention is relevant with a kind of fluid treating device, in processing unit (plant), quality improvement is disposed, such as polluting water purification, the activation of water, the improvement quality of flow-like oil or the purification of exhaust and after handling, water and oil mix and form a kind of emulsion fuel as a result.
Recently, be combined under the far infrared band irradiation of electromagnetic waves such as the low molecular weight polycaprolactone of water, oil or class quasi-fluid and mix, thereby and grain refine promptly activate the quality of drinking-water and flow-like oil improved.In the case, formerly have in the Technology in Japan patent 1622923, the inventor provides the continuous poriferous Web materials of being made by pottery can be used as filter element effectively.
Because of these filtration members embrittlements,, can stop up gradually so be used in the cylinder that is under the closed state, under situation such as the wet goods viscous liquid, stop up and to become obvious especially, to light oil after 20 to 30 hours, heavy oil after 4 to 5 hours, is stopped up and occurs in the inflow side.The exhaust that also has internal combustion engine also can take place to stop up in early days and be difficult to tackle under the low situation of 200 ℃ to 300 ℃ temperature.The problem that exists also comprises the honeycombed catalyst that is difficult to effectively tackle at present.
The purpose of this invention is to provide a kind of fluid can be smoothly by and the fluid management device that is connected with a filtration members securely simultaneously, even also can reduce to stop up and safeguard easily to viscous liquid, thereby just can obtain the purification of industrial wastewater, the activation of drinking-water, the efficiency of combustion that fuel oil is good and further preventing the pollution of the environment.
Another object of the present invention is the fine mixing of water and oil and processing and forms a kind of emulsion.
Therefore, the present invention puts having a fluid processing cartridge that has the perforation helix tube at the center, have the threaded hole passage and the netted continuous poriferous filtration members that is that is enclosed in the through hole of guiding the through hole periphery into, this helix tube and filtration members are all made with a resistive heater by ceramic material and be used for heating on the concave surfaces in the helix tube outside, have that envelope can install and be enclosed in the cylinder that links to each other with the helix tube of the through hole of filtration members and a kind of heat exchanger fluid or heat-exchange gas can be filled in the helix tube outside and circulate between the cylinder to be used for heating with linking to each other.
Relevant operation of the present invention, because liquid can not only be by being netted continuous poriferous filtration members and can flowing along the outer peripheral face that helix tube provides, occur in the filtration members inflow side even stop up, fluid also can pass the spiral through-hole passage and be input to the helix tube inboard, also be that the tapped through hole passage becomes a bypass, and the fluid that is eddy flow is latticed filtration members from multi-direction entering, thereby pass continuous poriferous filtration members, this just obtains good processing contact-making surface expansion and safe fluid.
If a resistive heater is used for heating or a kind of heat exchanger fluid or gas on the concave surface in the helix tube outside and is full of the helix tube outside and institute and connects and also mobilely betwixt between the cylinder be used for heating, to be processedly can improve such as such its flowability of viscous liquid of oil.Particularly when handling exhaust,, and under high pressure produce a large amount of NO in diesel engine because the oxygen surplus may take place x(nitrogen oxide) is because the relationship between quality of fuel oil produces free carbon through regular meeting, if pass helix tube and filtration members along with activity improves these materials, at 500 ℃ of-700 ℃ of temperature, CO, CH, C, NO xAnd O 2Between oxygen exchange come to life because reaction heat does not rely on the heat of input from the outside, reaction is proceeded because the path of spiral through hole, the gas of the quick eddy flow that becomes enters netted filtration members and diffusion within it, reaction is maintained and strengthens.Because reacting to each other under normal pressure, the under high pressure NO of Chan Shenging xReduce because of changing nitrogen into, and the material of discharging all becomes H 2O, CO 2, N 2, so just can obtain the protection of environment.
In about 5 kilograms per centimeter 2Pressure under spray into water and oil and pass a continuous porous filtering spare, thereby formed fuel combination.Use this kind fuel, shorten in the length of flame of stove internal combustion, furnace temperature descends about 300 ℃, at this moment NO xBe reduced to about 1/4 with the CO amount.
Fig. 1 is the longitudinal sectional view of one embodiment of the invention;
Fig. 2 is the transverse sectional view of the embodiment of the invention;
Fig. 3 is that the expression ceramic mud injects the longitudinal sectional view under the mould internal state;
To be the expression ceramic mud discharge and adhere to longitudinal sectional view under a mould and the reticulate body state from a plaster mold to Fig. 4;
Fig. 5 takes off the longitudinal sectional view that the mould rear section is dissectd before being illustrated in burning under the molding state;
Fig. 6 is the longitudinal sectional view of another embodiment.
Hereinafter will be described in detail with regard to one embodiment of the invention illustrated in figures 1 and 2.One helix tube of being made by pottery 1 has a through hole 11 at the center, and a spiral through-hole passage 12 is led to the periphery of through hole 11 and through-hole passage 120 enlarges in inflow side and outflow side, and dwindles again in end, inflow side 121 and end, outflow side 122.
One is in the through hole 11 that netted continuous poriferous ceramic filter spare 2 is enclosed in helix tube 1.The filtration members that forms wherein is immersed in the ceramic liquid and carries out drying by burning reticulate body that material makes, burns by roasting then, and one is netted continuous porous body is then formed by the ceramic segment of remainder.
Helix tube 1 is such formation, and promptly ceramic mud becomes mould and roasting in the suction plaster mold that separates.
As shown in Figure 3, a reticulate body that can burn 6 is encapsulated in the through hole 51 of plaster mold 5, and spiral through-hole passage 52 is arranged on the periphery of central through hole 51, and ceramic mud and adhere to the interior week and the reticulate body 6 of mould 5, the demoulding then reinjects.Thereby as shown in Figure 4, die casting goes out a tubular piece that has the formed space of spiral through-hole passage, carries out drying roasting then again.As shown in Figure 5,6 of reticulate bodies are burnt and the continuous poriferous filtration members 2 of the ceramic material that formed by remaining ceramic segment integrally is encapsulated in the through hole 11, thereby made the helix tube of a ceramic material, its thickness can suitably be chosen, and this depends on its adhesion time.
In addition, filtration members 2 before the roasting and the helix tube 1 before the roasting can be made separately, and filtration members 2 just is encapsulated in the through hole of helix tube 1, filtration members 2 and helix tube 1 together roasting so that make overall structure.
In making filtration members 2 processes, in helix tube, produce many apertures so by burning reticulate body, on the other hand, helix tube is immersed in the ceramic mud once more and is being full of roasting again under the situation of aperture, thus the intensity of reticulate body filtration members 2 also just increases at this moment.Again during roasting, the lid 13 that is positioned at a side can bond and go up and carry out roasting.
Filtration members 2 and helix tube 1 also can be distinguished roasting, and filtration members 2 can be encapsulated in the through hole 11 of helix tube 1, or the filtration members 2 of roasting can be encapsulated in the unfired helix tube 1, subsequently roasting helix tube and making again.
One resistive heater 3 is wrapped on each corresponding outer concave surface of helix tube 1, and it is interior and be provided with bottom 14 as whole component parts that a cylinder 4 is installed and be encapsulated in to helix tube 1.
Hereinafter will narrate the action of this embodiment.Water or oil are from covering 121 inputs of 13 inflow end, pass filtration members 2 and through-hole passage 12, discharge from the outflow end part 122 of bottom 14, in the case, water or oil are cleaned and improve quality by passing the contact of being carried out between helix tube 1 and the ceramic filtration members of making 2.
In this embodiment, even stop up in filtration members 2, water or oil pass through-hole passage 12 and the bypass blocking portion, can guarantee that water or oil flow smoothly thereby enter filtration members 2 from another angle.
Again because heater strip 3 on each corresponding outer concave surface 13 of helix tube 1, has heated helix tube 1 self and filtration members, thereby with the energy of electromagenetic wave radiation and conductive form transmission, from helix tube 1 and filtration members 2 inputs, this has just strengthened water and oily activity.If the fluid that purifies is a viscous liquid a kind of as oil, also has the effect that flowability improves and make to stop up by heating and reduce.In addition, because described cylinder 4, thereby heat insulating ability improves and has improved the shock resistance characteristic and protected helix tube 1 and filtration members 2.
And, water and oil inject down and by continuous poriferous filtration members 2 about 5 kilograms/centimeter 2 pressure, by the pressure that is acted on from ceramic far infrared radiation influence, make the water of quick swirling motion and the particle of oil and be filtered part mixing and stirring, under good interaction, just can obtain fuel combination, mixed content just can be made the fuel combination of smooth combustion up to 50% water, use this fuel combination, compare significantly with 100% astatki in the length of flame of stove internal combustion and to shorten, furnace temperature reduces about 300 ℃, NO xIt is about 1/4 that (nitrogen oxide) and CO (carbon monoxide) also drop to, and also detects less than HC at stove exit.Therefore, using the internal-combustion steam engine of emulsion fuel, can utilize the pressure that oxidized produces and improve the efficient of fuel, also air conservation significantly simultaneously.
Narration has above constituted embodiments of the invention, yet the present invention is not limited thereto embodiment is as long as the technology modification within the scope that claim is protected all is included within the present invention.
For example, no matter the material of characteristics such as helix tube and netted filtering spare have such as hear resistance with what material and shaping, and be anticorrosive all is suitable for, so long as material has good electromagenetic wave radiation characteristic and good heat-resisting and anticorrosion properties, wherein pottery is only material.Equally, the shape of cross section that centers on the spiral through-hole passage of through hole periphery is not placed restrictions on, in addition, corresponding its purposes of the pitch of spiral through hole can be arbitrarily, and such as being used for purification, activation, this type of the fluid management of improving the quality also is arbitrarily, and as shown in Figure 6, the gas such as exhaust flows into and flows out part and all freely opens.
When the helix tube fit on and be encapsulated in the cylinder that is connected, connect cylinder material or shape be arbitrarily.When filtration members is heated, except resistive heater, also can fill with a kind of heat exchanger fluid or as the heat-exchange gas of steam and the outside of helix tube and connected between the cylinder and circulated.
According to the present invention because fluid can not only be in netted filtering spare by and also can also pass through along the helix tube of guiding the outer peripheral face that centers on into.Stop up even produce in filtration members, fluid also can pass the spiral through-hole passage and send, and the result just can filter to high-quality smoothly.
In claim 2 or the described fluid processing cartridge of claim 3 were put, because this device is to be made by pottery, so the energy of electromagnetic radiation and the hot form of conduction is easy to accept, the fluid management such as the liquid activation also can strengthen.
In claim 4, because helix tube and the filtration members made by pottery are that whole die casting is shaped, molding becomes easy like this.
In claim 5, durability is protected and improved to a helix tube, and in claim 6, along with improving durability, the disposal of fluid then further strengthens.
In claim 7,, improve and can guarantee that it flows smoothly such as the flowability of the viscous liquid of oils because a filtration members and a helix tube are heated.
In claim 8 and 9, the circulation by a kind of heat exchanger fluid or be filled in the helix tube outside and connect between the cylinder, filtration members and helix tube can be easy to be heated so.

Claims (9)

1. a fluid treating device has:
A helix tube is drilled with a through hole in the central and the spiral through-hole passage of guiding into around above-mentioned through hole periphery is arranged.
The one continuous poriferous filtration members that is netted state is encapsulated in the described through hole.
2. a kind of fluid treating device according to claim 1 is characterized in that continuous poriferous filtration members is to be made by pottery.
3. a kind of fluid treating device according to claim 1 is characterized in that helix tube made by pottery.
4. a kind of fluid treating device according to claim 1, it is characterized in that the reticulate body that can burn is encapsulated in the through hole at a mould center, this mould has a spiral through-hole passage on the through hole periphery, die casting subsequently and roasting one are made in the through hole that the continuous poriferous filtration members that is netted state integrally is encapsulated in the helix tube that pottery makes by pottery as a result.
5. a kind of fluid treating device according to claim 1 is characterized in that the helix tube that filtration members is encapsulated in the through hole is installed and is encapsulated in the cylinder that links to each other.
6. a kind of fluid treating device according to claim 1 is characterized in that the helix tube of being made by pottery that the filtration members that pottery is made is encapsulated in the through hole is installed and is encapsulated in the cylinder that links to each other.
7. a kind of fluid treating device according to claim 1 is characterized in that a heater strip is wrapped on the concave surface in the helix tube outside.
8. a kind of fluid treating device according to claim 5 is characterized in that a kind of heat exchanger fluid or a kind of heat-exchange gas are filled between the helix tube outside and the continuous cylinder and circulate.
9. according to claim 7 or the described a kind of fluid treating device of claim 8, it is characterized in that a kind of heat exchanger fluid or a kind of heat-exchange gas are filled between the helix tube outside and the continuous cylinder and circulate.
CN94115657A 1994-09-05 1994-09-05 Fluid processing device Expired - Fee Related CN1063982C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN94115657A CN1063982C (en) 1994-09-05 1994-09-05 Fluid processing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN94115657A CN1063982C (en) 1994-09-05 1994-09-05 Fluid processing device

Publications (2)

Publication Number Publication Date
CN1118280A true CN1118280A (en) 1996-03-13
CN1063982C CN1063982C (en) 2001-04-04

Family

ID=5037618

Family Applications (1)

Application Number Title Priority Date Filing Date
CN94115657A Expired - Fee Related CN1063982C (en) 1994-09-05 1994-09-05 Fluid processing device

Country Status (1)

Country Link
CN (1) CN1063982C (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI391613B (en) * 2009-04-16 2013-04-01 Japan Environmental Preservation Co Ltd A mixture of emulsion combustion and a mixed liquid supply system for emulsion combustion
CN101815745B (en) * 2007-10-04 2013-04-10 新日本石油株式会社 Antiblocking-agent masterbatch and polyolefin resin film produced with the same
CN103301666A (en) * 2013-07-04 2013-09-18 姚力芝 Multifunctional water purifier
CN108097648A (en) * 2016-11-25 2018-06-01 宁德市凯欣电池材料有限公司 Material wash mill
CN108236850A (en) * 2016-12-27 2018-07-03 黑龙江吉纳森生物工程股份有限公司 A kind of molten gas mixer of eddy current type and its application
CN109695442A (en) * 2017-12-05 2019-04-30 安徽省睿斯达石油有限公司 One kind is allied the communists the spiral pressure break liquid mixing system of formula
CN114768579A (en) * 2022-05-19 2022-07-22 北京科技大学 Pre-stirring equipment before alloy solution pouring

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0777041B2 (en) * 1987-07-20 1995-08-16 キヤノン株式会社 Optical recording medium with protective member and optical recording / reading method thereof

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101815745B (en) * 2007-10-04 2013-04-10 新日本石油株式会社 Antiblocking-agent masterbatch and polyolefin resin film produced with the same
TWI391613B (en) * 2009-04-16 2013-04-01 Japan Environmental Preservation Co Ltd A mixture of emulsion combustion and a mixed liquid supply system for emulsion combustion
CN103301666A (en) * 2013-07-04 2013-09-18 姚力芝 Multifunctional water purifier
CN103301666B (en) * 2013-07-04 2014-12-10 姚力芝 Multifunctional water purifier
CN108097648A (en) * 2016-11-25 2018-06-01 宁德市凯欣电池材料有限公司 Material wash mill
CN108097648B (en) * 2016-11-25 2021-02-12 宁德市凯欣电池材料有限公司 Material washing device
CN108236850A (en) * 2016-12-27 2018-07-03 黑龙江吉纳森生物工程股份有限公司 A kind of molten gas mixer of eddy current type and its application
CN109695442A (en) * 2017-12-05 2019-04-30 安徽省睿斯达石油有限公司 One kind is allied the communists the spiral pressure break liquid mixing system of formula
CN114768579A (en) * 2022-05-19 2022-07-22 北京科技大学 Pre-stirring equipment before alloy solution pouring
CN114768579B (en) * 2022-05-19 2023-10-13 北京科技大学 Pre-stirring equipment before pouring alloy solution

Also Published As

Publication number Publication date
CN1063982C (en) 2001-04-04

Similar Documents

Publication Publication Date Title
US5259190A (en) Heated cellular structures
AU607882B2 (en) Muffler apparatus with filter trap and method of use
DE60016218T2 (en) DEVICE AND METHOD FOR REMOVING RUSSIAN PARTICLES FROM EXHAUST GASES FROM COMBUSTION PROCESSES
EP0766993B1 (en) Filter for purifying exhaust gases
US5194078A (en) Exhaust filter element and exhaust gas-treating apparatus
US4867768A (en) Muffler apparatus with filter trap and method of use
US5065576A (en) Exhaust gas purifying device for a diesel engine
CN100383366C (en) Ceramic honeycomb filter and exhaust gas-cleaning method
EP1149232B1 (en) Integrated apparatus for removing pollutants from a fluid stream in a lean-burn environment with heat recovery
KR100747088B1 (en) Dpf with improving heat durability
US5575904A (en) Fluid processing device with filter in helical channel tube
CN1063982C (en) Fluid processing device
JPH0160652B2 (en)
CN2821170Y (en) Diesel engine exhaust regeneration filter purifying silensing device
US7892308B2 (en) Ceramic filter
EP0443625B1 (en) Exhaust filter element and exhaust gas-treating apparatus
DE10350264A1 (en) Catalyst temperature control by microwave induced particle oxidation
DE4224172C2 (en) Gas cleaning device
BRPI0618308A2 (en) refractory discharge filtration method and device
JPH01252588A (en) Cellular fiber ceramic body and waste gas filter using said body
CH678020A5 (en) Diesel motor catalyst filter - has channels with electric heating to give reaction temp. for catalyst action
CN107269347A (en) Plugged Honeycomb Structure
JPH07328445A (en) Catalytic composition for removing particulate substance of diesel vehicle
JPS5791726A (en) Exhaust gas filter for internal-combustion engine
DE4433028C2 (en) Fluid treatment device

Legal Events

Date Code Title Description
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C06 Publication
PB01 Publication
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20010404

Termination date: 20100905