CN104016373A - Heat self-exchange tube array fin dual ammonia preparation device - Google Patents
Heat self-exchange tube array fin dual ammonia preparation device Download PDFInfo
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- CN104016373A CN104016373A CN201410227464.6A CN201410227464A CN104016373A CN 104016373 A CN104016373 A CN 104016373A CN 201410227464 A CN201410227464 A CN 201410227464A CN 104016373 A CN104016373 A CN 104016373A
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- absorption
- heat
- reactor
- ammonia
- tubulation
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Abstract
The invention discloses a heat self-exchange tube array fin dual ammonia preparation device, which is mainly composed of two absorption reactors. The inside of each absorption reactor can closely contact with the outer wall of a liquid ammonia steel cylinder, so that the liquid ammonia steel cylinder can be contained between the two absorption reactors; and array tubes and fins are arranged in the two absorption reactors. In the ammonia preparation process, the heat released from the absorption reaction can simultaneously absorbed by the liquefied ammonia gasification process through the array tubes and fins in the reactors, so as to reach the purpose of dual exchange of array tubes and fins; heat released from the reaction process is effectively removed, and heat required by liquid ammonia gasification is supplied, so as to facilitate the proceeding of the reaction towards the product generation direction as well as supply stable gasification temperature for liquid ammonia; and heat direct self-exchange of heat released in the absorption reaction and heat absorbed by liquid ammonia gasification in the system is realized, so that the ammonia preparation process is carried out and completed under efficient and stable conditions without the need of cooling water and electricity.
Description
Technical field
The invention belongs to chemical production equipment and Chemicals preparing technical field, especially relate to a kind of without water coolant, without the heat self-exchange tubulation fin double-type ammoniacal liquor preparation facilities of electricity consumption.
Background technology
Ammoniacal liquor is the important reagent in laboratory, and the GB content of reagent ammoniacal liquor is 25%.The industrial reductive agent as flue gas desulfurization and denitrification.In agricultural, after dilution, can be used as chemical fertilizer.Inorganic industry is selected various molysite for system.In military affairs as a kind of alkaline sterilizing agent, for the sarin class toxic agent of sterilizing.The industry such as wool spinning, silk, printing and dyeing are used for washing wool, woollen goods, grey cloth, and dissolve and adjust potential of hydrogen, and as dyeing auxiliaries etc.Organic industry, as aminating agent, is produced the catalyzer of heat-reactive phenolic resin.Pharmaceutically with weak ammonia, breathing and the reflectivity that circulated are stimulated, cure and fall in a swoon and faint, and make dermerethistica and Herb of Common violet.Also as washing composition, neutralizing agent, alkaloid leaching agent.Also for pharmaceutical industry, blueprint etc.
Ammoniacal liquor is prepared ultimate principle: the aqueous solution of the water-soluble formation of ammonia is called ammoniacal liquor.Its reaction equation is: NH
3+ H
2o → NH
3h
2o.Ammonia dissolves readily in water.In the time of 20 ℃, the terminate an agreement ammonia of 700 volumes of the water soluble of a volume.From chemical equilibrium viewpoint, NH3 (gas)+H2O (liquid)=NH
3h
2o+Q, this reaction is reversible exothermic reaction.In adiabatic process, along with the carrying out of reaction process, the temperature of solution increases, and backward reaction speed strengthens, the content of balance ammonia declines, when solution temperature rises to 35 ℃, under 1 normal atmosphere, solution-stabilized ammonia content is 25%, when temperature is during higher than 35 ℃, under 1 normal atmosphere, the content of solution-stabilized ammonia is just less than 25%, and at 1 normal atmosphere, solution temperature is higher than being to produce qualified ammoniacal liquor in 35 ℃ of situations.Therefore, in producing ammoniacal liquor process, must remove in time institute's liberated heat in reaction process, production operation is controlled in the situation that 1 normal atmosphere is less than 35 ℃ and carry out.
In industrial production, to be that water carries out cooling for reaction process institute liberated heat, its operation is that ammonia is supplied with by liquid ammonia steel bottle, and liquid ammonia steel bottle is controlled by envrionment temperature, liquefied ammonia endothermic gasification, pass in absorption reactor thermally and react, in reaction process, with water coolant, remove heat, reaction process is normally carried out.But, because envrionment temperature is very unstable, it is different along with the difference in season, in one day along with transformation temperature early, middle and late, night alters a great deal, therefore, the liquid ammonia gasification speed in liquid ammonia steel bottle is also large with variation of ambient temperature, namely in reactor, enters ammonia amount and fluctuates larger, in the constant situation of water coolant, make the temperature variation in absorption reactor thermally also large.In addition water coolant used along with source difference, season and difference early, middle and late, night, cooling water inlet temperature rangeability is also larger, this also directly affects the temperature of reaction in reactor.Because temperature in absorption reactor thermally produces large fluctuation, its result, not only affects the stable of quality product, and causes a large amount of wastes of ammonia, and the utilization ratio of ammonia is significantly declined, and causes environmental pollution, to operation, brings very large difficulty.
At present, the preparation technology of ammoniacal liquor mainly contains: bubble absorption, bubble-plate column absorb and the direct absorption process of liquefied ammonia.CN2873744Y utility model discloses a kind of device for quick preparing industrial ammonia water, adopt a plurality of interchanger, reasonable arrangement ammonia solution runner and water medium runner, make full use of the heat absorption and release in ammoniacal liquor preparation process, in a unit equipment, increase to greatest extent heat interchanging area, improve heat transfer effect, complete repeatedly absorption reaction.CN201148352Y utility model discloses a kind of device of preparing ammoniacal liquor, has greatly shortened the preparation time of ammoniacal liquor, has reduced production cost, has also avoided atmospheric pollution, has improved production operation environment.CN101863495B disclosure of the invention a kind of equipment that efficiently liquefied ammonia and water is configured to ammoniacal liquor, overcome that prior art ammoniacal liquor allocative efficiency is low, configuration required equipment is many, noise greatly, the defect such as finished product ammonia concn is low, ammonia concn is inhomogeneous.CN201940202U utility model discloses a kind of device of being prepared ammoniacal liquor by liquefied ammonia, for liquefied ammonia and water, be mixed with the problem that ammoniacal liquor process exists, overcome process noise and vibration problems, solve the problem of hot ammoniacal liquor simultaneously, a kind of efficient, stable and reliable device of being prepared ammoniacal liquor by liquefied ammonia is provided.CN102701233B disclosure of the invention a kind of liquefied ammonia resorber and ammoniacal liquor preparation system thereof, a kind of liquefied ammonia resorber is provided, adopt the direct absorption process of novel liquefied ammonia to prepare ammoniacal liquor, its support equipment is few, its system used device is few, and technique is simple, and self-produced ammoniacal liquor comprehensive cost is low.CN203183930U discloses a kind of ammoniacal liquor preparation facilities, provide a kind of ammonia concn evenly, good cooling results, the saving energy, safe and reliable ammoniacal liquor preparation facilities.CN202336300U utility model discloses a kind of ammonia device of releasing, and has technical process cylinder list and easily operates, and ammonia concn is even and can control as required outlet ammonia concn, ammonia rate of loss is lower, have fewer environmental impacts, can move continuously, production efficiency advantages of higher.CN103285755A disclosure of the invention a kind of coil tube type ammoniacal liquor prepare all-in-one, there is reasonable in design, processing safety is high, ammonia concn is even, save energy, the loss of ammonia is less, little to environmental influence, can move continuously, compact construction, the advantage such as heat exchange efficiency is high, more convenient to operate.
Above technical scheme has all been made in various degree and having been improved for original different technologies defect, but all depart from water coolant, do not remove this link of reaction process release of heat, still exist liquid ammonia gasification speed in liquid ammonia steel bottle with entering in variation of ambient temperature, absorption reactor thermally in the fluctuation of ammonia amount, absorption reactor thermally to produce the problems such as temperature fluctuation and water resources and energy dissipation.
Summary of the invention
Technical problem to be solved by this invention, according to emitting heat in the water-soluble reaction process of ammonia, and in liquid ammonia gasification process, absorb this mechanism of heat, the heat absorbing while taking ammoniacal liquor to prepare absorption reaction liberated heat and liquid ammonia gasification carries out the method mutually directly exchanging voluntarily, the heat that both reaction process can have been produced is removed, guarantee that absorption reaction carries out to the direction of product generation, can supply with again the stable gasification temperature of liquid ammonia gasification, a kind of heat self-exchange tubulation fin double-type ammoniacal liquor preparation facilities is provided.
Realizing technical scheme of the present invention is: a kind of heat self-exchange tubulation fin double-type ammoniacal liquor preparation facilities, mainly by two absorption reactor thermallies, formed, the inner side of described two absorption reactor thermallies be tubular semicircle can with liquid ammonia steel bottle outer wall close contact, can be by liquid ammonia steel bottle double team in the middle of two absorption reactor thermallies; One side of described absorption reactor thermally is connected by rotating shaft, and the universal wheel that can move it is equipped with in absorption reactor thermally bottom, and two absorption reactor thermallies can be done folding by rotating shaft and move, and can make liquid ammonia steel bottle put into easily or take out in the middle of two absorption reactor thermallies; Tubulation and fin are equipped with in described absorption reactor thermally inside, inlet pipe is also housed and is attached thereto the gas dispersion pipe connecing; In ammoniacal liquor preparation process, liquid ammonia gasification becomes ammonia to absorb heat by tubulation first to make the pure water in reactor lower the temperature, then ammonia enters reactor and pure water generation absorption reaction by gas dispersion pipe, the heat that absorption reaction produces is except being absorbed by tubulation, the fin and the inwall that are absorbed in reactor conduct on the liquid ammonia steel bottle in the middle of two absorption reactor thermallies simultaneously, gasification by liquefied ammonia in steel cylinder absorbs, and reaches the object of tubulation and the dual heat-shift of fin; Both effectively remove reaction process institute liberated heat, constantly supplied with again the required heat of liquid ammonia gasification, and be not only conducive to the direction that reaction generates to product and carry out, and provided stable gasification temperature for liquefied ammonia; Realize the directly exchange voluntarily of the heat release of absorption reaction and the heat absorption of liquid ammonia gasification heat in system, made ammoniacal liquor preparation process carry out and complete under efficient, stable, not need cooling power and water condition.
Tubulation intake valve, tubulation air outlet valve, reactor intake valve, reactor vent valve are equipped with in the top of described two absorption reactor thermallies, and reactor liquid feed valve is equipped with in side, and reactor liquid-outlet valve is equipped with in bottom; The fin that be equipped with absorption reactor thermally inside is distributed on absorption reactor thermally inwall, and welds mutually with absorption reactor thermally inwall; The gas dispersion pipe that be equipped with absorption reactor thermally inside is placed in absorption reactor thermally bottom, is distributed with the aperture of emission gases on gas dispersion pipe.
The beneficial effect that the present invention produces is:
1. realize the directly exchange voluntarily of the heat release of absorption reaction and the heat absorption of liquid ammonia gasification heat in system, made ammoniacal liquor preparation process carry out and complete in efficient, stable, energy-conservation system.Having effectively utilized system self emits and the heat energy absorbing, avoided the impact of variation of ambient temperature, improved the stability of reaction process in reaction system, ammoniacal liquor production is stablized to be carried out normally, thereby guaranteed quality product, saved cooling water resources and saved mechanical water pump and the input of electric energy.
2. with heat self-exchange tubulation fin double-type ammoniacal liquor preparation facilities of the present invention, produce ammoniacal liquor, the vaporization temperature of liquefied ammonia and the temperature in absorption reactor thermally are adapted, the total absorptivity of ammonia can be brought up to more than 98%, greatly reduces ammonia consumption, has improved quality product, easy and simple to handle, equipment is simple, has not only improved operational condition, has reduced environmental pollution, and the effective and reasonable energy that utilizes, significantly improved economic benefit and social benefit.
Accompanying drawing explanation
Fig. 1 is structure drawing of device of the present invention.
Embodiment
For understanding that can be detailed to the present invention, according to embodiment, be also described in further detail by reference to the accompanying drawings.As shown in Figure 1, absorption reactor thermally 1 of the present invention is mainly the semicircular absorption reactor thermally 1-1 of tubular, 1-2 by two inner sides and forms, and 1-1 is as one-level absorption reactor thermally, and 1-2 is as secondary absorption reactor thermally; The inner side of two absorption reactor thermallies can with the outer wall close contact of liquid ammonia steel bottle 2, and by liquid ammonia steel bottle 2 double teams in the middle of 1-1,1-2 two-stage absorption reactor thermally; One side of two-stage absorption reactor thermally is connected by rotating shaft 1-3, the universal wheel 1-7 that can move it is equipped with in two-stage absorption reactor thermally bottom, two-stage absorption reactor thermally can be done folding by rotating shaft and move, and can make liquid ammonia steel bottle 2 put into easily or take out in the middle of two absorption reactor thermally 1-1 and 1-2; Tubulation 1-1-7 and fin 1-1-10 are equipped with in absorption reactor thermally inside, inlet pipe 1-1-8 is also housed and is attached thereto the gas dispersion pipe 1-1-9 connecing.
The 1-3 of during production, two absorption reactor thermally 1-1 and 1-2 being take opens to both sides as rotating shaft, and liquid ammonia steel bottle 2 is placed between two absorption reactor thermallies and by absorption reactor thermally and is merged; By the 1-1-5 of absorption reactor thermally side, the pure water that 1-2-5 reactor liquid feed valve passes into absorption reactor thermally volume 2/3～3/4; Gas duct 1-4 is connected with the gas phase cylinder valve 2-1 of liquid ammonia steel bottle 2 and the tubulation intake valve 1-1-1 at one-level absorption reactor thermally top, gas duct 1-5 is connected with reactor intake valve 1-1-3 with tubulation air outlet valve 1-1-2, gas duct 1-6 is connected with the reactor vent valve 1-1-4 of one-level absorption reactor thermally 1-1 and the reactor intake valve 1-2-3 of secondary absorption reactor thermally 1-2; Open successively vent valve 1-2-4, the intake valve 1-2-3 of secondary absorption reactor thermally 1-2, the vent valve 1-1-4 of one-level absorption reactor thermally 1-1, tubulation air outlet valve 1-1-2, reactor intake valve 1-1-3, tubulation intake valve 1-1-1, and the gas phase cylinder valve 2-1 of liquid ammonia steel bottle 2; Liquefied ammonia starts gasification, and ammonia disperses to enter in water to be absorbed generation ammoniacal liquor by water through the aperture of gas duct 1-4, tubulation 1-1-7, reactor inlet pipe 1-1-8, gas dispersion pipe 1-1-9, meanwhile the heat of tubulation absorption reaction system; The heat that the heat that absorption reaction produces also will absorb during by liquid ammonia steel bottle 2 liquid ammonia vaporization of close contact with it by the fin 1-1-10 in absorption reactor thermally and inwall exchanges, thereby both reached, remove the heat that reaction process produces, and provided again liquid ammonia gasification required gasification temperature.
Ammonia is after one-level absorption reactor thermally major part is absorbed, and a small amount of unabsorbed ammonia enters secondary absorption reactor thermally 1-2 through vent valve 1-1-4, airway 1-6, reactor intake valve 1-2-3, again with water generation absorption reaction; Degree of absorption in one-level absorption reactor thermally 1-1 reaches after requirement, closes the gas phase cylinder valve 2-1 of liquid ammonia steel bottle 2, and the tapping valve 1-1-6 that opens one-level absorption reactor thermally emits finished product ammoniacal liquor.Refill pure water in one-level absorption reactor thermally 1-1, gas duct 1-4 is connected on the gas phase cylinder valve 2-1 of liquid ammonia steel bottle 2 and the tubulation intake valve 1-2-1 of secondary absorption reactor thermally 1-2, gas duct 1-5 is connected on the reactor intake valve 1-1-3 of one-level absorption reactor thermally 1-1 and the reactor vent valve 1-2-4 of secondary absorption reactor thermally 1-2, gas duct 1-6 is connected on the tubulation air outlet valve 1-2-2 and reactor intake valve 1-2-3 of secondary absorption reactor thermally 1-2, be about to second reactor and change A reactor into, A reactor originally changes second reactor into, proceed absorption reaction.
Below, for produce the comparison of ammoniacal liquor output with absorption reaction device of the present invention and general method, for the liquid ammonia steel bottle of 800 liters, its maximum filling weight is 400 kilograms, the ammoniacal liquor that production ammonia quantity is 25%.
| Production method | The total absorptivity of ammonia | Every bottle of liquefied ammonia amount usable | Ammoniacal liquor output (25%) | Water coolant | Water pump | Electricity |
| The inventive method | 98％ | 392 kilograms | 1568 kilograms | × | × | × |
| General method | 60％ | 240 kilograms | 960 kilograms | √ | √ | √ |
Find out thus with heat self-exchange tubulation fin double-type ammoniacal liquor preparation facilities of the present invention and produce ammoniacal liquor, utilize the mutual exchange of self energy effective and reasonablely, not only improved liquefied ammonia utilization ratio, increased the output of ammoniacal liquor, and saved cooling water resources, and save the input of mechanical water pump and electric energy, improve operational condition, reduced the environmental pollution that exhaust emissions causes, there is significant economic benefit and social benefit.
Claims (4)
1. a heat self-exchange tubulation fin double-type ammoniacal liquor preparation facilities, mainly by two absorption reactor thermallies, formed, it is characterized in that: the inner side of described two absorption reactor thermallies be tubular semicircle can with liquid ammonia steel bottle outer wall close contact, can be by liquid ammonia steel bottle double team in the middle of two absorption reactor thermallies; One side of described absorption reactor thermally is connected by rotating shaft, and the universal wheel that can move it is equipped with in absorption reactor thermally bottom, and two absorption reactor thermallies can be done folding by rotating shaft and move, and can make liquid ammonia steel bottle put into easily or take out in the middle of two absorption reactor thermallies; Tubulation and fin are equipped with in described absorption reactor thermally inside, inlet pipe is also housed and is attached thereto the gas dispersion pipe connecing; In ammoniacal liquor preparation process, liquid ammonia gasification becomes ammonia to absorb heat by tubulation first to make the pure water in reactor lower the temperature, then ammonia enters reactor and pure water generation absorption reaction by gas dispersion pipe, the heat that absorption reaction produces is except being absorbed by tubulation, the fin and the inwall that are absorbed in reactor conduct on the middle liquid ammonia steel bottle of two absorption reactor thermallies simultaneously, gasification by liquefied ammonia in steel cylinder absorbs, and reaches the object of tubulation and the dual heat-shift of fin; Both effectively remove reaction process institute liberated heat, constantly supplied with again the required heat of liquid ammonia gasification, and be not only conducive to the direction that reaction generates to product and carry out, and provided stable gasification temperature for liquefied ammonia; Realize the directly exchange voluntarily of the heat release of absorption reaction and the heat absorption of liquid ammonia gasification heat in system, made ammoniacal liquor preparation process carry out and complete under efficient, stable, not need cooling power and water condition.
2. according to the heat self-exchange tubulation fin double-type ammoniacal liquor preparation facilities described in right 1, tubulation intake valve, tubulation air outlet valve, reactor intake valve, reactor vent valve are equipped with in the top of described two absorption reactor thermallies, reactor liquid feed valve is equipped with in side, and reactor liquid-outlet valve is equipped with in bottom.
3. according to the heat self-exchange tubulation fin double-type ammoniacal liquor preparation facilities described in right 1, the fin that be equipped with described absorption reactor thermally inside is distributed on absorption reactor thermally inwall, and welds mutually with absorption reactor thermally inwall.
4. according to the heat self-exchange tubulation fin double-type ammoniacal liquor preparation facilities described in right 1, the gas dispersion pipe that be equipped with described absorption reactor thermally inside is placed in absorption reactor thermally bottom, is distributed with the aperture of emission gases on gas dispersion pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410227464.6A CN104016373B (en) | 2014-05-22 | 2014-05-22 | Heat self-exchange tubulation fin double-type ammoniacal liquor preparation facilities |
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|---|---|---|---|
| CN201410227464.6A CN104016373B (en) | 2014-05-22 | 2014-05-22 | Heat self-exchange tubulation fin double-type ammoniacal liquor preparation facilities |
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|---|---|
| CN104016373A true CN104016373A (en) | 2014-09-03 |
| CN104016373B CN104016373B (en) | 2016-02-10 |
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|---|---|---|---|
| CN201410227464.6A Expired - Fee Related CN104016373B (en) | 2014-05-22 | 2014-05-22 | Heat self-exchange tubulation fin double-type ammoniacal liquor preparation facilities |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104190214A (en) * | 2014-09-17 | 2014-12-10 | 南京凯盛国际工程有限公司 | Ammonia gas absorbing device |
| CN111533766A (en) * | 2020-03-25 | 2020-08-14 | 中棉小康生物科技有限公司 | Ethephon rearrangement process |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3295927A (en) * | 1965-10-21 | 1967-01-03 | Phillips Petroleum Co | Aqua ammonia production |
| CA2452244A1 (en) * | 2003-01-09 | 2004-07-09 | Rocky Research | Ammonia-water absorption system with plunger-driven diaphragm solution pump |
| CN2873744Y (en) * | 2006-03-21 | 2007-02-28 | 任翱翔 | Device for quick preparing industrial ammonia water |
| CN201372209Y (en) * | 2009-01-20 | 2009-12-30 | 天津渤天化工有限责任公司 | Overspeed reaction ammonia absorber |
| CN101863495A (en) * | 2009-06-10 | 2010-10-20 | 北京九州美电科技有限公司 | Equipment for efficiently preparing ammonia water from liquid ammonia and water |
| CN203183930U (en) * | 2013-04-18 | 2013-09-11 | 天津奥利环保设备有限公司 | Ammonia water preparation device |
| CN203329626U (en) * | 2013-06-24 | 2013-12-11 | 天津市奥利达设备工程技术有限公司 | Coil pipe type ammonia water preparation integrated machine |
| CN203922750U (en) * | 2014-05-22 | 2014-11-05 | 李景峰 | Heat self-exchange tubulation fin double-type ammoniacal liquor preparation facilities |
-
2014
- 2014-05-22 CN CN201410227464.6A patent/CN104016373B/en not_active Expired - Fee Related
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3295927A (en) * | 1965-10-21 | 1967-01-03 | Phillips Petroleum Co | Aqua ammonia production |
| CA2452244A1 (en) * | 2003-01-09 | 2004-07-09 | Rocky Research | Ammonia-water absorption system with plunger-driven diaphragm solution pump |
| CN2873744Y (en) * | 2006-03-21 | 2007-02-28 | 任翱翔 | Device for quick preparing industrial ammonia water |
| CN201372209Y (en) * | 2009-01-20 | 2009-12-30 | 天津渤天化工有限责任公司 | Overspeed reaction ammonia absorber |
| CN101863495A (en) * | 2009-06-10 | 2010-10-20 | 北京九州美电科技有限公司 | Equipment for efficiently preparing ammonia water from liquid ammonia and water |
| CN203183930U (en) * | 2013-04-18 | 2013-09-11 | 天津奥利环保设备有限公司 | Ammonia water preparation device |
| CN203329626U (en) * | 2013-06-24 | 2013-12-11 | 天津市奥利达设备工程技术有限公司 | Coil pipe type ammonia water preparation integrated machine |
| CN203922750U (en) * | 2014-05-22 | 2014-11-05 | 李景峰 | Heat self-exchange tubulation fin double-type ammoniacal liquor preparation facilities |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104190214A (en) * | 2014-09-17 | 2014-12-10 | 南京凯盛国际工程有限公司 | Ammonia gas absorbing device |
| CN111533766A (en) * | 2020-03-25 | 2020-08-14 | 中棉小康生物科技有限公司 | Ethephon rearrangement process |
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| Publication number | Publication date |
|---|---|
| CN104016373B (en) | 2016-02-10 |
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