KR920703452A - 염화 칼슘과 아세틸렌의 제조를 위한 2-단 공정 - Google Patents

염화 칼슘과 아세틸렌의 제조를 위한 2-단 공정

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Publication number
KR920703452A
KR920703452A KR1019920701016A KR920701016A KR920703452A KR 920703452 A KR920703452 A KR 920703452A KR 1019920701016 A KR1019920701016 A KR 1019920701016A KR 920701016 A KR920701016 A KR 920701016A KR 920703452 A KR920703452 A KR 920703452A
Authority
KR
South Korea
Prior art keywords
reaction
calcium
reaction vessel
calcium chloride
water
Prior art date
Application number
KR1019920701016A
Other languages
English (en)
Other versions
KR950010805B1 (ko
Inventor
더블유.벙어 제임스
류 호일
데비네니 프라새드 에이.브이
Original Assignee
로날드 제이.퍼그마이어
유니버시티 오브 유타
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 로날드 제이.퍼그마이어, 유니버시티 오브 유타 filed Critical 로날드 제이.퍼그마이어
Publication of KR920703452A publication Critical patent/KR920703452A/ko
Application granted granted Critical
Publication of KR950010805B1 publication Critical patent/KR950010805B1/ko

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00—Compounds of calcium, strontium, or barium
    • C01F11/02—Oxides or hydroxides
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00—Compounds of calcium, strontium, or barium
    • C01F11/20—Halides
    • C01F11/24—Chlorides
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00—Compounds of calcium, strontium, or barium
    • C01F11/20—Halides
    • C01F11/24—Chlorides
    • C01F11/28—Chlorides by chlorination of alkaline-earth metal compounds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10H—PRODUCTION OF ACETYLENE BY WET METHODS
    • C10H15/00—Acetylene gas generators with carbide feed, with or without regulation by the gas pressure
    • C10H15/06—Acetylene gas generators with carbide feed, with or without regulation by the gas pressure with automatic carbide feed by valves
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10H—PRODUCTION OF ACETYLENE BY WET METHODS
    • C10H3/00—Acetylene gas generators with automatic water feed regulation by means independent of the gas-holder

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

내용 없음.

Description

염화 칼슘과 아세틸렌의 제조를 위한 2-단 공정
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 탄화칼슘, 염화 수소와 물이 반응하여 아세틸렌과 염화칼슘을 형성하는 반응기 시스템을 나타낸 챠트이다.
제2도는 2-단 반응기 배치를 나타낸 챠트이다.

Claims (7)

  1. a.주반응 용기내에서 탄화칼슘과 과량의 물이 반응하여 아세틸렌가스와 수산화 칼슘을 형성하는 단계,b. 주반응 용기내에서 상기 반응이 60% 내지 90%로 달성이 진행되도록 하는 단계, c. 비반응된 물 및 탄화칼슘과 장입된 반응 생성물 아세틸렌 가스와 수산화칼슘을 제2반응용기로 운반시키는 단계, d. 제2반응 용기내에서 반응을 실질적으로 완결시키는 단계, e. 제2반응용기로 부터 아세틸렌 및 수산화 칼슘을 회수하는 단계로 이루어진 아세틸렌과 염화칼슘을 제조하기 위한 2-단 공정.
  2. 제1항에 있어서, 반응에 의해 생성된 수산화 칼슘은 중화기내에서 염화수소와 반응되어 회수되는 염화칼슘을 형성하는 것을 특징으로 하는 공정.
  3. 제1항에 있어서, 과량의 물과 탄화칼슘을 반응시키는 제1단계는 장입된 흐름-형태 반응기에서 수행되고, 반응을 완결시키는 제2단계는 조밀한 상의층류 플러그-흐름 형태의 반응기에서 수행되는 것을 특징으로 하는 공정.
  4. 제2항에 있어서, 염화칼슘은 건조기에서 건조되어 무수 염화 칼슘을 생성하는 것을 특징으로 하는 공정.
  5. 제4항에 있어서, 건조를 위해 필요한 열은 주 및 제2반응기 및 중화기에서 일어나는 반응으로 부터 유도하는 것을 특징으로 하는 공정.
  6. 제1항에 있어서, 주반응용기 내의 체류시간은 약1내지 3분인 것을 특징으로 하는 공정.
  7. 제1항에 있어서, 제2반응 용기내의 체류시간이 약30분 내지 2시간인 것을 특징으로 하는 공정.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019920701016A 1989-10-30 1990-10-25 아세틸렌 제조를 위한 장치 및 공정 KR950010805B1 (ko)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US43427089A 1989-10-30 1989-10-30
US434,270 1989-10-30
PCT/US1990/006149 WO1991006509A1 (en) 1989-10-30 1990-10-25 Two-stage process for production of calcium chloride and acetylene

Publications (2)

Publication Number Publication Date
KR920703452A true KR920703452A (ko) 1992-12-17
KR950010805B1 KR950010805B1 (ko) 1995-09-23

Family

ID=23723548

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019920701016A KR950010805B1 (ko) 1989-10-30 1990-10-25 아세틸렌 제조를 위한 장치 및 공정

Country Status (11)

Country Link
EP (1) EP0498844B1 (ko)
JP (1) JPH0645556B2 (ko)
KR (1) KR950010805B1 (ko)
AT (1) ATE110697T1 (ko)
AU (1) AU645043B2 (ko)
CA (1) CA2067815C (ko)
DE (1) DE69012140T2 (ko)
DK (1) DK0498844T3 (ko)
ES (1) ES2058940T3 (ko)
RU (1) RU2048505C1 (ko)
WO (1) WO1991006509A1 (ko)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2939132B1 (fr) * 2008-11-28 2011-11-11 Arkema France Fabrication de chlorure de vinyle monomere a partir de matieres renouvelables, chlorure de vinyle monomere obtenu et utilisation.
TWI478862B (zh) * 2009-06-04 2015-04-01 Voltaix Llc 用於製造三矽烷胺（ｔｒｉｓｉｌｙｌａｍｉｎｅ）之設備及方法
US11180371B2 (en) 2019-04-12 2021-11-23 J. Dustin Hultine Integrated synthesis of commodity chemicals from waste plastic

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE693064C (de) * 1936-10-01 1940-07-01 Linde Air Prod Co Verfahren und Vorrichtung zum Erzeugen von Acetylen und trockenem Calciumhydroxyd
US2701190A (en) * 1949-10-10 1955-02-01 Knapsack Ag Process for the continuous manufacture of acetylene
US2636807A (en) * 1951-10-09 1953-04-28 Gen Electric Purification of calcium chloride
US2951748A (en) * 1957-12-16 1960-09-06 Shawinigan Chem Ltd Acetylene generation
NL131806C (ko) * 1963-06-13
CH529693A (fr) * 1970-10-01 1972-10-31 Schaeffer Jean Rene Procédé de préparation de chlorure de calcium
US4451268A (en) * 1982-09-29 1984-05-29 Lerch John A Dry acetylene generator

Also Published As

Publication number Publication date
AU645043B2 (en) 1994-01-06
WO1991006509A1 (en) 1991-05-16
KR950010805B1 (ko) 1995-09-23
EP0498844A1 (en) 1992-08-19
EP0498844B1 (en) 1994-08-31
CA2067815A1 (en) 1991-05-01
DE69012140T2 (de) 1995-04-06
AU6725090A (en) 1991-05-31
DE69012140D1 (de) 1994-10-06
CA2067815C (en) 1998-12-22
EP0498844A4 (en) 1993-01-20
ES2058940T3 (es) 1994-11-01
JPH05500941A (ja) 1993-02-25
JPH0645556B2 (ja) 1994-06-15
DK0498844T3 (da) 1994-10-03
RU2048505C1 (ru) 1995-11-20
ATE110697T1 (de) 1994-09-15

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