JPH06136357A - Production of chemical heat-storage material - Google Patents

Production of chemical heat-storage material

Info

Publication number
JPH06136357A
JPH06136357A JP4210915A JP21091592A JPH06136357A JP H06136357 A JPH06136357 A JP H06136357A JP 4210915 A JP4210915 A JP 4210915A JP 21091592 A JP21091592 A JP 21091592A JP H06136357 A JPH06136357 A JP H06136357A
Authority
JP
Japan
Prior art keywords
ammonia
chemical heat
storage material
salt mixture
heat storage
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
JP4210915A
Other languages
Japanese (ja)
Other versions
JP3111667B2 (en
Inventor
Tomonari Saito
知成 斎藤
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.)
Nok Corp
Original Assignee
Nok Corp
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 Nok Corp filed Critical Nok Corp
Priority to JP04210915A priority Critical patent/JP3111667B2/en
Publication of JPH06136357A publication Critical patent/JPH06136357A/en
Application granted granted Critical
Publication of JP3111667B2 publication Critical patent/JP3111667B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To produce a chemical heat-storage material comprising an ammonia complex and having a controllable reaction temp. CONSTITUTION:An aq. soln. obtd. by completely dissolving CaCl2 and CaBr2 in water is concentrated and dried under heating and reduced pressure. To the resulting calcium salt mixture is added ammonia at about -20 deg.C under a pressure of ammonia gas of about 1.2atm to give a calcium salt mixture- ammonia complex, which is used as the chemical heat storage material.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】本発明は、化学蓄熱材の製造法に
関する。更に詳しくは、反応温度の制御が可能なアンモ
ニア錯体系化学蓄熱材の製造法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a chemical heat storage material. More specifically, the present invention relates to a method for producing an ammonia complex-based chemical heat storage material capable of controlling the reaction temperature.

【0002】[0002]

【従来の技術】CaCl2・nNH3(n=2,4,8)やCaBr2・nNH
3(n=2,6,8)などのアンモニア錯体は、それらのアンモ
ニア付加数の変化に伴う反応熱が非常に大きいことか
ら、熱の貯蔵やケミカルヒートポンプなどの化学蓄熱材
としての利用が図られている。
2. Description of the Related Art CaCl 2 ·nNH 3 (n=2, 4, 8) and CaBr 2 ·nNH
Ammonia complexes such as 3 (n = 2, 6, 8) are expected to be used as chemical heat storage materials such as heat storage and chemical heat pumps because the heat of reaction associated with the change in the number of ammonia additions is very large. It is

【0003】しかしながら、これらの化学蓄熱材のアン
モニア付加数が変化する反応温度は、化学蓄熱材の種
類、雰囲気中のアンモニアガス分圧などによって支配さ
れるため、ケミカルポンプなどを構成する際、その作動
温度や圧力の仕様に対して適した反応特性を有する化学
蓄熱材が存在しない場合がある。
However, the reaction temperature at which the ammonia addition number of these chemical heat storage materials changes is governed by the type of chemical heat storage material, the partial pressure of ammonia gas in the atmosphere, and the like. There may be no chemical heat storage material with suitable reaction characteristics for operating temperature and pressure specifications.

【0004】[0004]

【発明が解決しようとする課題】本発明の目的は、反応
温度の制御が可能なアンモニア錯体系化学蓄熱材の製造
法を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a method for producing an ammonia complex-based chemical heat storage material in which the reaction temperature can be controlled.

【0005】[0005]

【課題を解決するための手段】かかる本発明の目的は、
塩化カルシウムおよび臭化カルシウムを溶解させた水溶
液を濃縮、乾燥させて得られたカルシウム塩混合物無水
物にアンモニアを付加させて化学蓄熱材を製造すること
によって達成される。
DISCLOSURE OF THE INVENTION The object of the present invention is to:
This is achieved by adding ammonia to an anhydrous calcium salt mixture obtained by concentrating and drying an aqueous solution in which calcium chloride and calcium bromide are dissolved to produce a chemical heat storage material.

【0006】塩化カルシウム、臭化カルシウム共、無水
物、水和物のいずれをも使用することができる。本発明
方法においては、まず所定量の塩化カルシウムと臭化カ
ルシウムとを水に完全に溶解させた後、この水溶液を徐
々に加熱減圧下で濃縮し、溶解しているカルシウム塩混
合物を再び析出させ、析出残渣に水気がみられなくなっ
たところで、200℃前後の真空乾燥器内で24時間程度乾
燥させることが行われる。
[0006] Calcium chloride, calcium bromide, both anhydrides and hydrates can be used. In the method of the present invention, first, predetermined amounts of calcium chloride and calcium bromide are completely dissolved in water, and then this aqueous solution is gradually heated and concentrated under reduced pressure to reprecipitate the dissolved calcium salt mixture. After the deposition residue is no longer moist, it is dried in a vacuum dryer at around 200°C for about 24 hours.

【0007】得られたカルシウム塩混合物無水物に、ア
ンモニアガス圧約0.5〜2気圧、温度約-30〜20℃の条件
下でアンモニアを付加させると、どの混合比の場合に
も、CaCl2、CaBr2にそれぞれ8NH3が付加したものに相当
するカルシウム塩混合物アンモニア錯体が得られた。
[0007] When ammonia is added to the resulting anhydrous calcium salt mixture under conditions of ammonia gas pressure of about 0.5 to 2 atm and temperature of about -30 to 20°C, CaCl 2 and CaBr are produced at any mixing ratio. Calcium salt mixture ammonium complexes corresponding to the addition of 8NH3 to 2 respectively were obtained.

【0008】得られたカルシウム塩混合物アンモニア錯
体の脱NH3温度は、カルシウム塩の混合割合によっても
異なり、具体的には、アンモニアガス圧1.2気圧、温度-
20℃の条件下でアンモニア付加させたカルシウム塩混合
物アンモニア錯体の場合、次の表に示されるように、Ca
Cl2:CaBr2=50:50の混合モル比のとき、最も高い脱NH
3温度(アンモニアガス圧1気圧)を示している。 (以下余白) 表 混合モル比 8NH3錯体中の 脱NH3重量 脱NH3温度 CaCl2 CaBr2 NH3付加重量(%) (重量%) (℃) 100 0 55.1 27.6 30 (CaCl2・8NH3) (8NH3→4NH3) 90 10 53.2 27.1 34 80 20 51.3 26.3 36 70 30 50.0 26.0 38 60 40 48.1 23.8 39 50 50 46.5 21.1 40 40 60 45.1 17.2 39 30 70 43.9 14.1 37 20 80 42.6 12.1 34 10 90 41.5 10.5 32 0 100 40.5 10.1 26 (CaBr2・8NH3) (8NH3→6NH3) 注)8NH3錯体中のNH3付加重量:NH3付加重量/8NH3錯体
粉末重量 脱NH3重量:反応によって失われるNH3重量/8NH3錯体粉
末重量 脱NH3温度:NH3ガス圧1気圧下での脱NH3反応の反応平衡
温度
[0008] The deNH 3 temperature of the obtained calcium salt mixture ammonia complex also varies depending on the mixing ratio of the calcium salts.
In the case of the calcium salt mixture ammonia complex that was ammoniated under the condition of 20 °C, Ca
The highest deNH
3 Temperature (ammonia gas pressure 1 atm) is shown. (Blanks below) Table Mixing molar ratio De - NH3 weight in 8NH3 complex De - NH3 temperature CaCl2CaBr2NH3 addition weight (%) (% by weight) ( °C) ) (8NH 3 →4NH 3 ) 90 10 53.2 27.1 34 80 20 51.3 26.3 36 70 30 50.0 26.0 38 60 40 48.1 23.8 39 50 50 46.5 21.1 40 40 60 45.1 17.2 39 30 70 43.9 14.1 37 20 80 42.6 12.1 34 10 90 41.5 10.5 32 0 100 40.5 10.1 26 (CaBr 2 8NH 3 ) (8NH 3 → 6NH 3 ) Note) NH3 addition weight in 8NH3 complex: NH3 addition weight/ 8NH3 complex powder weight De - NH3 weight: Reaction NH3 weight/ 8NH3 complex powder weight lost by DeNH3 temperature: reaction equilibrium temperature of deNH3 reaction under NH3 gas pressure of 1 atm

【0009】これに対して、CaCl2(無水物)70モル%とCa
Br2(無水物)30モル%の粉末状態でのカルシウム塩混合物
について、アンモニアガス圧1.2気圧、温度-20℃でアン
モニア付加を行い、得られたカルシウム塩混合物アンモ
ニア錯体について、アンモニアガス圧1気圧での脱NH3
温度を測定すると、まず26℃では CaBr2・8NH3 → CaBr2・6NH3+2NH3 の反応分のNH3が脱離し、次いで30℃では CaCl2・8NH3 → CaCl2・4NH3+4NH3 の反応分のNH3が脱離した。即ち、粉末混合物をアンモ
ニア付加させたものの反応特性は、CaBr2・8NH3、CaCl2
・8NH3各成分単独の反応特性と何ら変わらない。
In contrast, 70 mol % CaCl 2 (anhydrous) and Ca
Br 2 (anhydride) 30 mol % powdery calcium salt mixture was subjected to ammonia addition at an ammonia gas pressure of 1.2 atm and a temperature of -20°C. DeNH3 at
When the temperature was measured, NH3 from the reaction of CaBr2.8NH3CaBr2.6NH3 + 2NH3 was first released at 26°C, and then CaCl2.8NH3CaCl2.4NH3 + 4NH at 30 °C. The reaction portion of 3 NH 3 was eliminated. That is, the reaction characteristics of the powder mixture added with ammonia are CaBr 2 .8NH 3 , CaCl 2
・The reaction characteristics of 8NH3 are not different from those of each component alone.

【0010】[0010]

【発明の効果】アンモニアガス圧1気圧における反応温
度は、 CaCl2・8NH3 ⇔ CaCl2・4NH3+4NH3 30℃ CaBr2・8NH3 ⇔ CaBr2・6NH3+2NH3 27℃ であるのに対し、水溶液状態を経て混合された塩化カル
シウム-臭化カルシウム混合物のアンモニア錯体は、そ
の脱NH3温度を混合比に応じて32〜40℃と高温側に最大1
0℃迄変化させることができ、反応温度の制御を可能と
させる。
[Effect of the Invention] The reaction temperature at an ammonia gas pressure of 1 atm is CaCl2.8NH3CaCl2.4NH3 + 4NH3 30 °C CaBr2.8NH3CaBr2.6NH3 + 2NH3 27°C. On the other hand, the ammonia complex of the calcium chloride-calcium bromide mixture mixed through the aqueous solution state has a deNH
It can be varied down to 0°C, making it possible to control the reaction temperature.

─────────────────────────────────────────────────────
──────────────────────────────────────────────────── ────

【手続補正書】[Written Amendment]

【提出日】平成4年10月8日[Submission date] October 8, 1992

【手続補正1】[Procedural amendment 1]

【補正対象書類名】明細書[Name of document to be amended] Description

【補正対象項目名】0003[Correction target item name] 0003

【補正方法】変更[Correction method] Change

【補正内容】[Correction details]

【0003】 しかしながら、これらの化学蓄熱材のア
ンモニア付加数が変化する反応温度は、化学蓄熱材の種
類、雰囲気中のアンモニアガス分圧などによって支配さ
れるため、ケミカルヒートポンプなどを構成する際、そ
の作動温度や圧力の仕様に対して適した反応特性を有す
る化学蓄熱材が存在しない場合がある。
[0003]However, the reaction temperature at which the number of additions of ammonia in these chemical heat storage materials changes is governed by the type of chemical heat storage material, the partial pressure of ammonia gas in the atmosphere, and the like. There may be no chemical heat storage material with suitable reaction characteristics for operating temperature and pressure specifications.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 塩化カルシウムおよび臭化カルシウムを
溶解させた水溶液を濃縮、乾燥させて得られたカルシウ
ム塩混合物無水物にアンモニアを付加させることを特徴
とする化学蓄熱材の製造法。
1. A method for producing a chemical heat storage material, comprising adding ammonia to a calcium salt mixture anhydride obtained by concentrating and drying an aqueous solution in which calcium chloride and calcium bromide are dissolved.
【請求項2】 請求項1記載の方法で得られたカルシウ
ム塩混合物アンモニア錯体。
2. A calcium salt mixture ammonia complex obtained by the method of claim 1.
JP04210915A 1992-07-15 1992-07-15 Manufacturing method of chemical heat storage material Expired - Fee Related JP3111667B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04210915A JP3111667B2 (en) 1992-07-15 1992-07-15 Manufacturing method of chemical heat storage material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04210915A JP3111667B2 (en) 1992-07-15 1992-07-15 Manufacturing method of chemical heat storage material

Publications (2)

Publication Number Publication Date
JPH06136357A true JPH06136357A (en) 1994-05-17
JP3111667B2 JP3111667B2 (en) 2000-11-27

Family

ID=16597174

Family Applications (1)

Application Number Title Priority Date Filing Date
JP04210915A Expired - Fee Related JP3111667B2 (en) 1992-07-15 1992-07-15 Manufacturing method of chemical heat storage material

Country Status (1)

Country Link
JP (1) JP3111667B2 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007307558A (en) * 2007-06-25 2007-11-29 Jfe Engineering Kk Adsorption/desorption agent, process for separation, and storage method for ammonia using combination of specific metal halides
JP2012082292A (en) * 2010-10-08 2012-04-26 Toyota Central R&D Labs Inc Chemical thermal storage medium and method for manufacturing the same
WO2012108343A1 (en) 2011-02-10 2012-08-16 株式会社豊田中央研究所 Chemical heat accumulator and method for producing same
WO2013027778A1 (en) * 2011-08-23 2013-02-28 株式会社豊田中央研究所 Chemical heat storage material, manufacturing method therefor and chemical heat storage structure
JP2014159497A (en) * 2013-02-19 2014-09-04 Toyota Central R&D Labs Inc Chemical heat storage material, method of producing the same and chemical heat storage structure
JP2015174783A (en) * 2014-03-14 2015-10-05 株式会社豊田中央研究所 Method for producing composite metal halide, and chemical heat storage material
WO2016059982A1 (en) * 2014-10-14 2016-04-21 株式会社豊田自動織機 Chemical heat storage device
US9914645B2 (en) 2013-11-07 2018-03-13 Regents Of The University Of Minnesota Process for making ammonia
WO2019042768A1 (en) * 2017-08-29 2019-03-07 Technische Universitaet Wien Method for thermo-chemical energy storage

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007307558A (en) * 2007-06-25 2007-11-29 Jfe Engineering Kk Adsorption/desorption agent, process for separation, and storage method for ammonia using combination of specific metal halides
JP2012082292A (en) * 2010-10-08 2012-04-26 Toyota Central R&D Labs Inc Chemical thermal storage medium and method for manufacturing the same
WO2012108343A1 (en) 2011-02-10 2012-08-16 株式会社豊田中央研究所 Chemical heat accumulator and method for producing same
WO2013027778A1 (en) * 2011-08-23 2013-02-28 株式会社豊田中央研究所 Chemical heat storage material, manufacturing method therefor and chemical heat storage structure
EP2749624A1 (en) * 2011-08-23 2014-07-02 Kabushiki Kaisha Toyota Chuo Kenkyusho Chemical heat storage material, manufacturing method therefor and chemical heat storage structure
JPWO2013027778A1 (en) * 2011-08-23 2015-03-19 株式会社豊田中央研究所 Chemical heat storage material, manufacturing method thereof, and chemical heat storage structure
EP2749624A4 (en) * 2011-08-23 2015-04-29 Toyota Chuo Kenkyusho Kk Chemical heat storage material, manufacturing method therefor and chemical heat storage structure
JP2014159497A (en) * 2013-02-19 2014-09-04 Toyota Central R&D Labs Inc Chemical heat storage material, method of producing the same and chemical heat storage structure
US9914645B2 (en) 2013-11-07 2018-03-13 Regents Of The University Of Minnesota Process for making ammonia
US10287173B2 (en) 2013-11-07 2019-05-14 Regents Of The University Of Minnesota Process for making ammonia
JP2015174783A (en) * 2014-03-14 2015-10-05 株式会社豊田中央研究所 Method for producing composite metal halide, and chemical heat storage material
JPWO2016059982A1 (en) * 2014-10-14 2017-06-08 株式会社豊田自動織機 Chemical heat storage device
WO2016059982A1 (en) * 2014-10-14 2016-04-21 株式会社豊田自動織機 Chemical heat storage device
WO2019042768A1 (en) * 2017-08-29 2019-03-07 Technische Universitaet Wien Method for thermo-chemical energy storage
AT520368A1 (en) * 2017-08-29 2019-03-15 Univ Wien Tech Process for thermochemical energy storage
AT520368B1 (en) * 2017-08-29 2022-12-15 Univ Wien Tech Process for thermochemical energy storage

Also Published As

Publication number Publication date
JP3111667B2 (en) 2000-11-27

Similar Documents

Publication Publication Date Title
JP7118514B2 (en) Use of compounds as energy materials
JPH06136357A (en) Production of chemical heat-storage material
CN106904583B (en) A kind of silicon nitride magnesium powder and preparation method thereof
CN110330462A (en) A kind of preparation method of 5- methyl tetrazolium metal complex containing energy
Dana et al. Thermal analysis of aqueous urea ammonium nitrate alternative fuel
US3926990A (en) Process for preparing amide polyphosphates
JP2012524011A (en) Manufacture of saturated ammonia storage materials
JPH0238577B2 (en)
JPS6259506A (en) Production of boron nitride
CN107651699A (en) A kind of production method of technical grade potassium nitrate
CN103864825A (en) Mixed ligand-based zinc complex and preparation method thereof
US20170066956A1 (en) Endothermic chemical reaction to remove heat
JPS62100404A (en) Production of pulverous hexagonal boron nitride having high purity
JP5439990B2 (en) Solid heavy metal treating agent, production method and use thereof
US3894017A (en) Preparation of alkali metal salts of dichloroisocyanuric acid
JPS60127285A (en) Manufacture of magnesia-containing granular composite fertilizer
JP2773920B2 (en) Method for producing tetraammine palladium (II) chloride
US3328129A (en) Production of boron carbide
JP3583170B2 (en) Gypsum manufacturing method
RU2116283C1 (en) Method of preparing water containing explosives
JP2529058B2 (en) Method for producing thermally expandable graphite
JPH0446884B2 (en)
US2544245A (en) Method for preparing dicyclohexylammonium nitrite
US3117839A (en) Method of preparing sorptive magnesia
CN105384661B (en) A kind of synthetic method of the triaminoguanidinium nitrate of suitable industrialized production

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees