1.
    发明专利
    未知

    公开(公告)号:RO79837A

    公开(公告)日:1983-02-01

    申请号:RO10072980

    申请日:1980-04-04

    Applicant: DEGUSSA

    Abstract: The known hydrocyanic acid-methane-ammonia (BMA) process for the production of hydrogen cyanide can now be carried out with liquified gases namely through the presence of additional hydrogen at the beginning of the reaction. The atomic ratio of carbon to nitrogen and hydrogen is from 1:1:7.1 to 1:1.33:13. As additional hydrogen there is the portion of hydrogen present coming out of the reaction "hydrocarbon+NH3". Otherwise the reaction conditions are the same as in the known BMA process.

    PROCESS FOR PRODUCING HYDROGEN CYANIDE

    公开(公告)号:CA1134593A

    公开(公告)日:1982-11-02

    申请号:CA349208

    申请日:1980-04-03

    Applicant: DEGUSSA

    Abstract: The BMA process, may also be carried out with liquefied gases, i.e., in the presence of additonal hydrogen at the start of the reaction. The atomic ratio of carbon to nitrogen to hydrogen is between 1:1:7.1 and 1:1.33:13. By additonal hydrogen is meant the portion exceeding the hydrogen present in the reaction according to the formula "KW + NH3". In all other respects the conditions of the reaction are the same as in the known BMA process.

    3.
    发明专利
    未知

    公开(公告)号:IT1127975B

    公开(公告)日:1986-05-28

    申请号:IT6704780

    申请日:1980-01-14

    Applicant: DEGUSSA

    Abstract: The known hydrocyanic acid-methane-ammonia (BMA) process for the production of hydrogen cyanide can now be carried out with liquified gases namely through the presence of additional hydrogen at the beginning of the reaction. The atomic ratio of carbon to nitrogen and hydrogen is from 1:1:7.1 to 1:1.33:13. As additional hydrogen there is the portion of hydrogen present coming out of the reaction "hydrocarbon+NH3". Otherwise the reaction conditions are the same as in the known BMA process.

    METHOD OF PREPARATION OF THE HYDROGEN CYANIDE

    公开(公告)号:CS211369B2

    公开(公告)日:1982-02-26

    申请号:CS218580

    申请日:1980-03-08

    Applicant: DEGUSSA

    Abstract: The known hydrocyanic acid-methane-ammonia (BMA) process for the production of hydrogen cyanide can now be carried out with liquified gases namely through the presence of additional hydrogen at the beginning of the reaction. The atomic ratio of carbon to nitrogen and hydrogen is from 1:1:7.1 to 1:1.33:13. As additional hydrogen there is the portion of hydrogen present coming out of the reaction "hydrocarbon+NH3". Otherwise the reaction conditions are the same as in the known BMA process.

    5.
    发明专利
    未知

    公开(公告)号:DD149654A5

    公开(公告)日:1981-07-22

    申请号:DD21994780

    申请日:1980-03-26

    Applicant: DEGUSSA

    Abstract: The known hydrocyanic acid-methane-ammonia (BMA) process for the production of hydrogen cyanide can now be carried out with liquified gases namely through the presence of additional hydrogen at the beginning of the reaction. The atomic ratio of carbon to nitrogen and hydrogen is from 1:1:7.1 to 1:1.33:13. As additional hydrogen there is the portion of hydrogen present coming out of the reaction "hydrocarbon+NH3". Otherwise the reaction conditions are the same as in the known BMA process.

    6.
    发明专利
    未知

    公开(公告)号:MX153268A

    公开(公告)日:1986-09-05

    申请号:MX18091280

    申请日:1980-01-22

    Applicant: DEGUSSA

    Abstract: The known hydrocyanic acid-methane-ammonia (BMA) process for the production of hydrogen cyanide can now be carried out with liquified gases namely through the presence of additional hydrogen at the beginning of the reaction. The atomic ratio of carbon to nitrogen and hydrogen is from 1:1:7.1 to 1:1.33:13. As additional hydrogen there is the portion of hydrogen present coming out of the reaction "hydrocarbon+NH3". Otherwise the reaction conditions are the same as in the known BMA process.

    7.
    发明专利
    未知

    公开(公告)号:IT8067047D0

    公开(公告)日:1980-01-14

    申请号:IT6704780

    申请日:1980-01-14

    Applicant: DEGUSSA

    Abstract: The known hydrocyanic acid-methane-ammonia (BMA) process for the production of hydrogen cyanide can now be carried out with liquified gases namely through the presence of additional hydrogen at the beginning of the reaction. The atomic ratio of carbon to nitrogen and hydrogen is from 1:1:7.1 to 1:1.33:13. As additional hydrogen there is the portion of hydrogen present coming out of the reaction "hydrocarbon+NH3". Otherwise the reaction conditions are the same as in the known BMA process.

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