CN106063982A - A kind of vegetable active flame-retarding fire-extinguishing agent producing process - Google Patents
A kind of vegetable active flame-retarding fire-extinguishing agent producing process Download PDFInfo
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- CN106063982A CN106063982A CN201610369949.8A CN201610369949A CN106063982A CN 106063982 A CN106063982 A CN 106063982A CN 201610369949 A CN201610369949 A CN 201610369949A CN 106063982 A CN106063982 A CN 106063982A
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- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D1/00—Fire-extinguishing compositions; Use of chemical substances in extinguishing fires
- A62D1/0028—Liquid extinguishing substances
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Abstract
nullThe present invention relates to a kind of vegetable active flame-retarding fire-extinguishing agent producing process，Comprise the following steps: from No. 3 storage tanks, produce liquid by No. 1 reactor of water pipe suction by the A group that pump handle is quantitative，Utilize hot and cold water blood circulation that temperature of liquid in still is controlled between 20 35 DEG C，In No. 2 storage tanks, extract quantitative B group produce liquid to No. 1 reactor，Stir 15 minutes with adjustable frequency motor，From No. 2 reactors, extract quantitative C group produce in liquid to No. 1 reactor，Stir 10 minutes，It is warming up to 40 45 DEG C by hot water cyclesystem after the xanthan gum that artificial input is quantitative，Insulated and stirred 60 minutes，The most manually pour quantitative AE0 9 insulated and stirred into 130 minutes，Then it is cooled to less than 40 DEG C by cold water circulating system，Stablize 48 hours，Detect qualified after，With water pump, synthesis liquid is extracted to No. 1 storage tank，Finally pack warehouse-in，Preparation is simple，Environment friendly and pollution-free，Raw material is easy to get，Equipment investment is few，Purity is high，Convenient to operate，Pollute little，Without at high pressure、Carry out under high temperature.
Description
Technical field
The present invention relates to extinguishing chemical technical field, particularly relate to a kind of vegetable active flame-retarding fire-extinguishing agent producing process.
Background technology
Owing to the processing technology of current fire retardant is the most traditional, need to carry out in the case of high pressure, high temperature, make on the market
The fire retardant made, not only when making, has big pollution, and the purity simultaneously produced and efficiency all compare lowly, therefore, it is difficult to
Meet human wants.
Summary of the invention
Present situation to above-mentioned prior art, the technical problem to be solved be to provide a kind of pollute little, without
The vegetable active flame-retarding fire-extinguishing agent producing process carried out under high pressure, high-temperature condition.
The present invention solves the technical scheme that above-mentioned technical problem used: a kind of vegetable active fire retardant extinguisher produces work
Skill, comprises the following steps: produces liquid by the A group that pump handle is quantitative from No. 3 storage tanks and passes through in No. 1 reactor of water pipe suction, profit
By hot and cold water blood circulation, temperature of liquid in still is controlled between 20-35 DEG C, in No. 2 storage tanks, extract quantitative B group produce
In liquid to No. 1 reactor, stir 15 minutes with adjustable frequency motor, from No. 2 reactors, extract quantitative C group produce liquid to No. 1
In reactor, stir 10 minutes, be warming up to 40-45 DEG C by hot water cyclesystem after the xanthan gum that artificial input is quantitative, insulation
Stir 60 minutes, more manually pour quantitative AEO-9 insulated and stirred into 130 minutes, be then cooled to 40 by cold water circulating system
Below DEG C, stablize 48 hours, detect qualified after, with water pump will synthesis liquid extract to No. 1 storage tank, finally pack warehouse-in.
Further, the production technology of described A group comprises the following steps: under the conditions of natural temperature, and artificial addition is quantitatively
Plant ash, by water pipe, quantitative tap water is injected in leaching pond, after naturally drenched, stir 60 points with air agitator
Clock.It is stirred for 60 minutes after standing 24 hours afterwards.Again after standing 38 hours, with immersible pump by the water pipe of closing by clear liquid
(immersible pump water inlet band drainage screen) is delivered in No. 3 storage tanks standby, and remaining plant ash residue then packs delivers to chemical fertilizer factory.
Further, the production technology of described B group comprises the following steps: by water pipe, quantitative tap water is injected No. 4
In reactor, under adjustable frequency motor stirs, utilize hot water cyclesystem that the tap water in reactor is warming up to 38-43 DEG C,
Manually add quantitative tween 80 insulation (38-43 DEG C) to stir 30 minutes, add quantitative Radix Artemisia ordosicae insulation (38-43 DEG C) and stir 5
Minute, add quantitative HUANGSONG insulation (38-43 DEG C) and stir 5 minutes, add quantitative Fructus Gleditsia insulation (38-43 DEG C) and stir 5 points
Clock, adds quantitative Cortex ulmi pumilae insulation (38-43 DEG C) and stirs 10 minutes, be warming up to 45-50 DEG C of insulation again and stir after soaking 4 hours
Mix 100 minutes, be then cooled to 35 DEG C by cold water circulating system, natural sedimentation 24 hours, afterwards the B group in still is produced liquid
By water pump in water pipe is delivered to No. 2 storage tanks standby.Open reactor bottom valve (built-in drainage screen), residue is poured into specially
With recycling bin, periodically deliver to chemical fertilizer factory.
Further, the production technology of described C group comprises the following steps: by hot and cold water blood circulation by No. 4 reactors
Middle temperature of liquid controls between 18-35 DEG C, by water pump, the A group being stored in No. 3 storage tanks is produced liquid and is injected into 4 through water pipe
In number reactor, artificial put into quantitative sodium benzoate, stir 100 minutes with motor, add quantitative distiller grains and stir 130 points
Clock, after soaking 48 hours, produces liquid the A group in No. 4 reactors and is delivered in No. 2 reactors standby by water pump.Open anti-
Answer still bottom valve, residue is put into recycling bin, then delivers to chemical fertilizer factory by special-purpose vehicle.
Compared with prior art, it is an advantage of the current invention that: one vegetable active flame-retarding fire-extinguishing agent producing process of the present invention
Preparing convenient and simple, environment friendly and pollution-free, raw material is easy to get, and equipment investment is few, and purity is high, it is simple to operation, pollutes little, it is not necessary at height
Carrying out under pressure, high temperature, the present invention is reasonable in design, can large-scale promotion.
Accompanying drawing explanation
Fig. 1 is one vegetable active fire retardant extinguisher production technological process one of the present invention；
Fig. 2 is one vegetable active fire retardant extinguisher production technological process two of the present invention；
Fig. 3 is one vegetable active fire retardant extinguisher production technological process three of the present invention；
Fig. 4 is one vegetable active fire retardant extinguisher production technological process four of the present invention.
Detailed description of the invention
In order to make the purpose of the present invention, technical scheme and advantage clearer, below in conjunction with accompanying drawing, the present invention is entered
Row further describes.
As Figure 1-4, a kind of vegetable active flame-retarding fire-extinguishing agent producing process, comprise the following steps: use from No. 3 storage tanks
The quantitative A group of pump handle produces liquid by, in No. 1 reactor of water pipe suction, utilizing hot and cold water blood circulation temperature of liquid in still
Control between 20-35 DEG C, in No. 2 storage tanks, extract quantitative B group produce liquid to No. 1 reactor, stir with adjustable frequency motor
Mixing 15 minutes, extract quantitative C group and produce in liquid to No. 1 reactor, stir 10 minutes from No. 2 reactors, artificial input is determined
It is warming up to 40-45 DEG C by hot water cyclesystem after the xanthan gum of amount, insulated and stirred 60 minutes, more manually pour quantitative AEO-into
9 insulated and stirred 130 minutes, are then cooled to less than 40 DEG C by cold water circulating system, stablize 48 hours, detect qualified after, use
Synthesis liquid is extracted to No. 1 storage tank by water pump, finally packs warehouse-in.
Further, the production technology of described A group comprises the following steps: under the conditions of natural temperature, and artificial addition is quantitatively
Plant ash, by water pipe, quantitative tap water is injected in leaching pond, after naturally drenched, stir 60 points with air agitator
Clock.It is stirred for 60 minutes after standing 24 hours afterwards.Again after standing 38 hours, with immersible pump by the water pipe of closing by clear liquid
(immersible pump water inlet band drainage screen) is delivered in No. 3 storage tanks standby, and remaining plant ash residue then packs delivers to chemical fertilizer factory.
Further, the production technology of described B group comprises the following steps: by water pipe, quantitative tap water is injected No. 4
In reactor, under adjustable frequency motor stirs, utilize hot water cyclesystem that the tap water in reactor is warming up to 38-43 DEG C,
Manually add quantitative tween 80 insulation (38-43 DEG C) to stir 30 minutes, add quantitative Radix Artemisia ordosicae insulation (38-43 DEG C) and stir 5
Minute, add quantitative HUANGSONG insulation (38-43 DEG C) and stir 5 minutes, add quantitative Fructus Gleditsia insulation (38-43 DEG C) and stir 5 points
Clock, adds quantitative Cortex ulmi pumilae insulation (38-43 DEG C) and stirs 10 minutes, be warming up to 45-50 DEG C of insulation again and stir after soaking 4 hours
Mix 100 minutes, be then cooled to 35 DEG C by cold water circulating system, natural sedimentation 24 hours, afterwards the B group in still is produced liquid
By water pump in water pipe is delivered to No. 2 storage tanks standby.Open reactor bottom valve (built-in drainage screen), residue is poured into specially
With recycling bin, periodically deliver to chemical fertilizer factory.
Further, the production technology of described C group comprises the following steps: by hot and cold water blood circulation by No. 4 reactors
Middle temperature of liquid controls between 18-35 DEG C, by water pump, the A group being stored in No. 3 storage tanks is produced liquid and is injected into 4 through water pipe
In number reactor, artificial put into quantitative sodium benzoate, stir 100 minutes with motor, add quantitative distiller grains and stir 130 points
Clock, after soaking 48 hours, produces liquid the A group in No. 4 reactors and is delivered in No. 2 reactors standby by water pump.Open anti-
Answer still bottom valve, residue is put into recycling bin, then delivers to chemical fertilizer factory by special-purpose vehicle.
Compared with prior art, it is an advantage of the current invention that: one vegetable active flame-retarding fire-extinguishing agent producing process of the present invention
Preparing convenient and simple, environment friendly and pollution-free, raw material is easy to get, and equipment investment is few, and purity is high, it is simple to operation, pollutes little, it is not necessary at height
Carrying out under pressure, high temperature, the present invention is reasonable in design, can large-scale promotion.
Claims (4)
1. a vegetable active flame-retarding fire-extinguishing agent producing process, it is characterised in that comprise the following steps: use water from No. 3 storage tanks
Pump produces liquid by, in No. 1 reactor of water pipe suction, utilizing hot and cold water blood circulation temperature of liquid control in still quantitative A group
System, between 20-35 DEG C, extracts quantitative B group in No. 2 storage tanks and produces liquid to No. 1 reactor, stir with adjustable frequency motor
15 minutes, extracting quantitative C group and produce in liquid to No. 1 reactor, stir 10 minutes from No. 2 reactors, artificial input is quantitatively
Xanthan gum after be warming up to 40-45 DEG C by hot water cyclesystem, insulated and stirred 60 minutes, more manually pour quantitative AEO-9 into
Insulated and stirred 130 minutes, is then cooled to less than 40 DEG C by cold water circulating system, stablizes 48 hours, detect qualified after, use water
Synthesis liquid is extracted to No. 1 storage tank by pump, finally packs warehouse-in.
A kind of vegetable active flame-retarding fire-extinguishing agent producing process the most according to claim 1, it is characterised in that described A group
Production technology comprises the following steps: under the conditions of natural temperature, artificial adds quantitative plant ash, by water pipe by quantitative from
Water is injected in leaching pond, stirs 60 minutes with air agitator after naturally drenched.It is stirred for 60 after standing 24 hours afterwards
Minute.Again after standing 38 hours, clear liquid (immersible pump water inlet band drainage screen) is carried by the water pipe closed with immersible pump
To No. 3 storage tanks standby, remaining plant ash residue then packs delivers to chemical fertilizer factory.
A kind of vegetable active flame-retarding fire-extinguishing agent producing process the most according to claim 1, it is characterised in that described B group
Production technology comprises the following steps: injects in No. 4 reactors by water pipe by quantitative tap water, stirs at adjustable frequency motor
Under, utilize hot water cyclesystem that the tap water in reactor is warming up to 38-43 DEG C, the tween 80 insulation that artificial addition is quantitative
(38-43 DEG C) stirs 30 minutes, adds quantitative Radix Artemisia ordosicae insulation (38-43 DEG C) and stirs 5 minutes, adds quantitative HUANGSONG insulation
(38-43 DEG C) stirs 5 minutes, adds quantitative Fructus Gleditsia insulation (38-43 DEG C) and stirs 5 minutes, adds quantitative Cortex ulmi pumilae and protect
Temperature (38-43 DEG C) stirs 10 minutes, is warming up to 45-50 DEG C of insulated and stirred again 100 minutes, then passes through cold water after soaking 4 hours
Cooling circulation system to 35 DEG C, natural sedimentation 24 hours, afterwards the B group in still is produced liquid and is delivered to 2 by water pump through water pipe
In number storage tank standby.Open reactor bottom valve (built-in drainage screen), residue is poured into Special recycling bin, periodically delivers to chemical fertilizer
Factory.
A kind of vegetable active flame-retarding fire-extinguishing agent producing process the most according to claim 1, it is characterised in that described C group
Production technology comprises the following steps: by hot and cold water blood circulation temperature of liquid in No. 4 reactors controlled 18-35 DEG C it
Between, the A group being stored in No. 3 storage tanks produced liquid in water pipe is injected into No. 4 reactors by water pump, artificial put into quantitative
Sodium benzoate, stirs 100 minutes with motor, adds quantitative distiller grains and stirs 130 minutes, after soaking 48 hours, No. 4 reactions
A group in still is produced liquid and is delivered in No. 2 reactors standby by water pump.Open reactor bottom valve, residue is put into back
Receive bucket, then deliver to chemical fertilizer factory by special-purpose vehicle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201610369949.8A CN106063982A (en) | 2016-05-31 | 2016-05-31 | A kind of vegetable active flame-retarding fire-extinguishing agent producing process |
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| CN201610369949.8A CN106063982A (en) | 2016-05-31 | 2016-05-31 | A kind of vegetable active flame-retarding fire-extinguishing agent producing process |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107050729A (en) * | 2017-06-21 | 2017-08-18 | 宁波水星环保科技有限公司 | A kind of preparation technology of plant composite fire-retardant extinguishing chemical |
| CN107050730A (en) * | 2017-06-21 | 2017-08-18 | 宁波水星环保科技有限公司 | A kind of high-efficiency environment friendly plant composite fire-retardant extinguishing chemical |
| CN107050728A (en) * | 2017-01-24 | 2017-08-18 | 嘉兴东日新材料科技股份有限公司 | Extinguishing chemical modifying agent and the plant modification extinguishing chemical comprising the modifying agent |
| CN107376182A (en) * | 2017-08-18 | 2017-11-24 | 高振芳 | A kind of graphene plant composite type fire retardant extinguisher |
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| US4950410A (en) * | 1988-12-30 | 1990-08-21 | United American, Inc. | Fire extinguishing compositions and methods |
| CN1086449A (en) * | 1988-12-27 | 1994-05-11 | 赵广生 | Plant liquid composite fire-retardant |
| CN1768878A (en) * | 2004-11-04 | 2006-05-10 | 济南广生生物活性研究所 | Plant and active water composite flame retardant extinguishing agent |
| CN101670161A (en) * | 2008-09-08 | 2010-03-17 | 刘泳 | Black nightshade herb biodegradation carbon-hydrogen fire extinguishing agent for firefighting and military shelters and method for processing same |
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2016
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| CN1086449A (en) * | 1988-12-27 | 1994-05-11 | 赵广生 | Plant liquid composite fire-retardant |
| US4950410A (en) * | 1988-12-30 | 1990-08-21 | United American, Inc. | Fire extinguishing compositions and methods |
| CN1768878A (en) * | 2004-11-04 | 2006-05-10 | 济南广生生物活性研究所 | Plant and active water composite flame retardant extinguishing agent |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107050728A (en) * | 2017-01-24 | 2017-08-18 | 嘉兴东日新材料科技股份有限公司 | Extinguishing chemical modifying agent and the plant modification extinguishing chemical comprising the modifying agent |
| CN107050728B (en) * | 2017-01-24 | 2021-12-03 | 嘉兴东日新材料科技股份有限公司 | Modifier for fire extinguishing agent and plant modified fire extinguishing agent containing same |
| CN107050729A (en) * | 2017-06-21 | 2017-08-18 | 宁波水星环保科技有限公司 | A kind of preparation technology of plant composite fire-retardant extinguishing chemical |
| CN107050730A (en) * | 2017-06-21 | 2017-08-18 | 宁波水星环保科技有限公司 | A kind of high-efficiency environment friendly plant composite fire-retardant extinguishing chemical |
| CN107376182A (en) * | 2017-08-18 | 2017-11-24 | 高振芳 | A kind of graphene plant composite type fire retardant extinguisher |
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Application publication date: 20161102 |
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